JPS59310A - Filter apparatus - Google Patents

Filter apparatus

Info

Publication number
JPS59310A
JPS59310A JP57109544A JP10954482A JPS59310A JP S59310 A JPS59310 A JP S59310A JP 57109544 A JP57109544 A JP 57109544A JP 10954482 A JP10954482 A JP 10954482A JP S59310 A JPS59310 A JP S59310A
Authority
JP
Japan
Prior art keywords
perforated plate
horizontal body
plate
fluid
cylindrical
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
Application number
JP57109544A
Other languages
Japanese (ja)
Other versions
JPS6015372B2 (en
Inventor
Manabu Oba
大羽 学
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP57109544A priority Critical patent/JPS6015372B2/en
Publication of JPS59310A publication Critical patent/JPS59310A/en
Publication of JPS6015372B2 publication Critical patent/JPS6015372B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Filtration Of Liquid (AREA)
  • Cyclones (AREA)

Abstract

PURPOSE:To provide a filter apparatus, constituted so as to prevent pressure loss therein and to act availably even if an inflow side comes to low pressure by such a mechanism that an outflow pipe is provided to the side surface of a tank main body so as to be positioned below an inflow pipe and a pressure difference reducing plate is concentriacally provided to the inside of a perforated plate arranged in the tank. CONSTITUTION:When a fluid is flowed into a tank main body 3 from an inflow pipe 15, heavy particles are separated and precipitated in a revolving stream space part 4 between the main body 3 and a perforated plate 5 and discharged from a discharge port 2 while light particles are separated by the perforated plate 5 to be removed from the fluid. In this case, the outflow pipe 16 of the fluid is provided below the inflow pipe 15 thereof to prevent pressure loss and an apparatus is availably acted. In addition, a pressure reducing plate 18 is concentrically provided to the inside of the perforated plate 5 through a gap 17 and a communication opening 30 is formed between the lower end thereof and the lower end of the perforated plate 5 to suppress the flow of the fluid passing the small orifices 6 of the perforated plate 5. By this constitution, the fluid is slowly flowed into the gap 17 and flowed out to the outflow pipe 16 through the communication opening 20.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は、たとえば河川から用水路に水を引込むときな
どに利用する濾過装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a filtration device used, for example, when drawing water from a river into an irrigation canal.

〔発明の技術的背景〕[Technical background of the invention]

本発明に技術的に近い従来例として、サイクロンがある
A cyclone is a conventional example that is technically close to the present invention.

一般的にこのサイクロンは、底部に沈降物排出口を有す
る円錐形の横本体と、この横本体の上部隔壁の中央に同
心状に設けた上下部開口の流出用円筒体と、横本体の上
部隔壁より下側に接線方向で接続したtAr、入・けと
を具備し、七うして、流体が横本体内に接線方向から流
入すると、その勢いで槽本体の内部に旋回流が生じ、比
較的厳い粒子等は、遠心力の作用で槽本体の内壁面側に
近づぎ、この晴本体の内壁面に沿って旋回しながら下降
して下部の沈降物排出口から断結的または連続的に取出
され、またこの重い粒子等を除去された比較的軽い粒子
等および流体は、槽本体の中央部を旋回しながら上昇し
、上部中央の流出用円筒体を経て外部に流出する。
Generally, this cyclone has a conical horizontal body with a sediment outlet at the bottom, an outflow cylinder with upper and lower openings provided concentrically in the center of the upper partition wall of the horizontal body, and an upper part of the horizontal body. It is equipped with an inlet and an inlet connected in a tangential direction below the partition wall, and when fluid flows into the horizontal body from a tangential direction, a swirling flow is generated inside the tank body due to its momentum. Tough particles approach the inner wall of the tank body due to the action of centrifugal force, descend while swirling along the inner wall of the tank body, and are discharged intermittently or continuously from the sediment discharge port at the bottom. The relatively light particles, etc., from which the heavy particles have been removed, and the fluid rise while swirling in the center of the tank body, and flow out through the outflow cylindrical body in the center of the upper part.

〔背景技術の問題点〕[Problems with background technology]

このようなサイクロンは、必ずηC5出口が流、入管よ
り上側に位置する構造であり、流入管に供給される流体
の圧力が高いときは有効に作用するが、流入管に供給さ
れるηを体の圧力が^くないとぎは内部での圧力ロスが
大きく、有効に作用しない問題点がある。
Such a cyclone has a structure in which the ηC5 outlet is always located above the flow and inlet pipes, and although it works effectively when the pressure of the fluid supplied to the inflow pipe is high, it does not absorb the η supplied to the inflow pipe. There is a problem that a knife without ^ pressure has a large internal pressure loss and does not work effectively.

そこで流出口を流入管よりも下方に設け、圧力1コスを
防ぐことが必要であるが、従来のサイクロン構造では、
それが不可能である。
Therefore, it is necessary to place the outlet below the inlet pipe to prevent 1 cos of pressure, but with the conventional cyclone structure,
That's not possible.

〔発明の目的〕[Purpose of the invention]

本発明は、サイクロンにおける旋回流による遠心分離作
用を利用しつつ、流出管を流入管よりも下方に設けて内
部での圧力ロスを防き、流入管側の圧力が比較的低圧の
場合でも有効に作用する濾過装置を提供しようとするも
のである。
The present invention makes use of the centrifugal separation effect caused by the swirling flow in the cyclone, and prevents internal pressure loss by providing the outflow pipe below the inflow pipe, making it effective even when the pressure on the inflow pipe side is relatively low. The purpose of the present invention is to provide a filtration device that acts on the following.

〔発明の概要〕[Summary of the invention]

1・1番目の本発明の構成は、底部に沈降物排出口を有
する円筒形の横本体と、この横本体の内部に旋回流窒間
部を介して同心状に設けられ局面に多数の小孔を有する
円筒形であって下部を開口しlこ多孔板と、この多孔板
の外周面に対応する範囲内で横本体の比較的上部の側面
に接線方向で接続した流入管と、上記多孔板の下部しi
口から横本体の比較的下部の側面を経て外部に引出した
流出管と、上記多孔板の内側に間隙を介して同心状に設
けられ下端と多孔板の下部との間に流通開口を形成する
円筒形の圧力差減少板とを具備したことを特徴とする1
過装置の構造に関−[るものであり、その作用は、流体
が横本体内に接線方向より血、入すると、その勢いで横
本体の内部に旋回b+tが生じ、比較的東い粒子環は、
旋(ロ)時に生ずる遠心力の作用で外側に分離され、横
本体の内壁面に浦って旋回しながら下降して槽本体の底
部に沈降し、また比較的軽いごみ停は多孔板によって1
遇され、この多孔板の小孔を通過した流体はtALl、
L1宮を経て外部に流出する。−り記比戦的軽いごみ寺
は、多孔板の外周面に清って旋回しながらその比重に応
じて下降または上昇して横本体の下部または上部に移動
するが、多孔板の内側に間隙を介し゛て同心状に設けた
圧力差減少板が多孔板の小孔を勢いよく通過しようとす
る流体の流れを抑制する作用があるから、多孔板の外側
部と内側部の間隙との間の圧力差が小さく維持され、こ
のため多孔板の外周面のごみ等は、多孔板の小孔に吸着
されにくいし、またこの多孔板の小孔に吸着されそうに
なるごみ等も旋回流によって多孔板から剥ぎとられ、多
孔板の目づまりが自然に解消され、多孔板は常に新鮮な
状態に保たれる。
1. The first structure of the present invention includes a cylindrical horizontal body having a sediment discharge port at the bottom, and a large number of small holes provided concentrically inside the horizontal body through a swirling nitrogen space. a cylindrical perforated plate having holes at its lower part; an inflow pipe connected tangentially to a relatively upper side surface of the horizontal body within a range corresponding to the outer peripheral surface of the perforated plate; The bottom of the board
A flow opening is formed between an outflow pipe drawn out from the mouth through a relatively lower side surface of the horizontal body, and a lower end of the perforated plate, which is provided concentrically with a gap interposed inside the perforated plate. 1 characterized in that it comprises a cylindrical pressure difference reducing plate.
This is related to the structure of the transverse body, and its action is that when fluid enters the horizontal body from a tangential direction, the momentum causes swirl b + t inside the horizontal body, and a relatively eastern particle ring is generated. teeth,
It is separated to the outside by the action of centrifugal force generated during rotation (b), descends while rotating on the inner wall surface of the horizontal body, and settles at the bottom of the tank body.
The fluid that passed through the small holes of this perforated plate is tALl,
It flows out through the L1 palace. - The comparatively light garbage temple moves around the outer peripheral surface of the perforated plate, descends or rises depending on its specific gravity, and moves to the lower or upper part of the horizontal body, but there is a gap inside the perforated plate. Since the pressure difference reducing plates arranged concentrically through the holes have the effect of suppressing the flow of fluid that tries to forcefully pass through the small holes of the perforated plate, the gap between the outer and inner parts of the perforated plate is reduced. The pressure difference between the two is maintained small, and therefore, dirt on the outer surface of the perforated plate is difficult to be absorbed by the small holes of the perforated plate, and dirt that is about to be absorbed by the small holes of the perforated plate is also absorbed by the swirling flow. It is peeled off from the perforated plate, the clogging of the perforated plate is naturally cleared, and the perforated plate is always kept in a fresh state.

またA−24目の本発明の構成は、上配才1査目の兄明
において、さらに多孔板の上部と横本体との間に浮上ご
みjII[1を設け、この浮上ごみ通口の上側に位置す
る液面レベルにおいて横本体の内側面に突部を設け、こ
の突部の下流側近傍において横本体に浮上ごみ取出し口
を鯨けたことを特徴とするf過装置の構造に関するもの
であり、その作用は、浮上ごみ通口を経て液面にずh上
した軽いごみは、横本体の側面に接線方向で接続した流
入管から槽本体の内部に流入する液体の旋回流とともに
液面で旋回しようとするが、上記突部を通過した後は、
との突部によって相対的に凹状となった突部の下流側に
生ずる渦流に引込まれて旋回流から分離し、この下流側
に設けられた浮上ごみ取出し口から液面部分の液ととも
に外部に排出される。
In addition, the configuration of the present invention in item A-24 is that, in the older brother of the first examiner, floating garbage jII [1 is further provided between the upper part of the perforated plate and the horizontal body, and the floating garbage jII [1] is provided above the floating garbage passage. This invention relates to the structure of an f-filtration device characterized in that a protrusion is provided on the inner surface of the horizontal body at a liquid level located at a liquid level located at The effect is that the light debris that has risen to the liquid surface through the floating debris port is raised to the liquid surface along with the swirling flow of the liquid that flows into the tank body from the inlet pipe connected tangentially to the side surface of the horizontal body. It tries to turn, but after passing the above protrusion,
It is drawn into the vortex generated on the downstream side of the relatively concave protrusion due to the protrusion, and is separated from the swirling flow. be discharged.

〔発明の実施例〕[Embodiments of the invention]

以下、本発明を図面に示す実施例をト照して詳細に説明
する。
Hereinafter, the present invention will be described in detail with reference to embodiments shown in the drawings.

3・1図および才2図に示す、l−1実施例のように、
紙部(1) K沈降物排出口(2)を有する円筒形の横
本体(3)の内部上側に、旋回流空間部(4)を介して
同心状に円筒形の多孔板(5)を設ける。この多孔板(
5)は、周面に多数の小孔(6)を有する円筒部の上端
を、槽本体(3)の上端閉塞部(力の中央開口部(8)
に固定される円板状の蓋(9)に固着するとともに、円
錐形下部(10)の下端を開口して下部開口(11)を
設けたものであり、全体を薄いスチール板によって成形
する。(12+は無(9)の取手である。
As in the l-1 embodiment shown in Figure 3.1 and Figure 2,
Paper part (1) A cylindrical perforated plate (5) is installed concentrically on the inside upper side of a cylindrical horizontal body (3) having a K-sediment discharge port (2) via a swirling flow space (4). establish. This perforated plate (
5) connects the upper end of the cylindrical part, which has a large number of small holes (6) on the circumferential surface, to the upper end closing part (center opening (8) of the tank body (3)).
It is fixed to a disc-shaped lid (9) that is fixed to the lid, and the lower end of the conical lower part (10) is opened to provide a lower opening (11), and the whole is molded from a thin steel plate. (12+ is the handle of nothing (9).

またこの多孔板(5)の外周面に対応する範囲内で横本
体(3)の比較的上部の側面に流入管a最を接線方向で
接続し、またL耐炎孔板(5)の下部開口aυかも横本
体(3)の比軟的下部の側面を経て外部に流出管この流
出管(16)の上端部に多孔&(5)の下部開口Uυを
着脱自在に嵌合する。
In addition, the inflow pipe a is tangentially connected to the relatively upper side surface of the horizontal body (3) within a range corresponding to the outer peripheral surface of the perforated plate (5), and the lower opening of the L flame-resistant perforated plate (5) is The outlet pipe (aυ) exits to the outside through the side surface of the relatively soft lower part of the horizontal body (3).The lower opening Uυ of the porous hole & (5) is removably fitted to the upper end of this outflow pipe (16).

また上記多孔板(5)の内t11]に間隙07)を介し
て同心状に円筒形の圧力差減少板Q81を設ける。この
圧力差減少板0樽は、−上端を上記蓋(9)に固層し、
下端を開口したもので、多孔板(5)に比べて充分な厚
みを有するスチール板によって成形する。そしてこの圧
力差減少板(18の下端四と多孔板(5)の円錐形下部
(1αとの間に流通開口(2flを形成する。
Further, a cylindrical pressure difference reducing plate Q81 is provided concentrically with the porous plate (5) inside t11 with a gap 07) therebetween. This pressure difference reducing plate 0 barrel has the upper end fixed to the lid (9),
It has an open bottom end and is formed from a steel plate that is thicker than the perforated plate (5). A communication opening (2fl) is formed between the lower end 4 of this pressure difference reducing plate (18) and the conical lower part (1α) of the perforated plate (5).

そうして、水、空気等の流体が流入管0団から横本体(
3)内に接線方向より流入ターると、その勢いにより、
横本体(3)と多孔板(5)との間の旋回流空間部(4
)で旋回流が生じ、比較的貞い粒子、胃こ等は、旋回時
に生ずる遠心力の作用で外側に分離され、底部(11に
沈降し、この横本体(3)の底部の沈降物排出口(2)
から図示しない開閉弁を経て外部に排出さj″j、また
比較的軽いごみ等は、多孔板(5)によってil−勺最
され、この多孔機(5)の小孔(6)を通過した流体は
、流出管(1句を経て外部に流出する。このようにして
、流体内の粒子、ごみ等を流体から有効に分離除去でき
るとともに、従来のサイクロンと異なり流出管Oeを流
入va最よりも下方に設けて圧力ロスを防ぐようにした
から、流入’su!9側の流体圧が比較的低圧の場合で
も本装置は有効に作用する。
Then, fluids such as water and air flow from the inflow pipe group 0 to the horizontal body (
3) When the inflow from the tangential direction inward, due to its momentum,
A swirling flow space (4) between the horizontal body (3) and the perforated plate (5)
), relatively clean particles such as stomach particles are separated to the outside by the action of centrifugal force generated during swirling, settle to the bottom (11), and are discharged from the bottom of the horizontal body (3). Exit (2)
From there, it is discharged to the outside via an on-off valve (not shown), and relatively light garbage, etc., is removed by a perforated plate (5) and passed through the small holes (6) of this perforated machine (5). The fluid flows out through the outflow pipe (1 line).In this way, particles, dirt, etc. in the fluid can be effectively separated and removed from the fluid, and unlike conventional cyclones, the outflow pipe Oe is connected to the inlet va end. 9 to prevent pressure loss, this device works effectively even when the fluid pressure on the inflow side is relatively low.

また上記比較的軽いごみ等は、多孔板(5)の外周面に
泊って旋回しながら七〇比電に応じて下降または上昇し
て横本体(3)の下部または上部に移動するが、多孔板
(5)の内側に間隙α力を介して同心状に設けられ下端
01と多孔板(5)の下部Qlとの間に流通開口−を形
成する円筒形の圧力差減少板081があるから、この圧
力差減少板(18が、多孔板(5)の小孔(6)を通過
しようとする流体の流れを抑制する作用があり、多孔板
(5)の外側部と内1Il11部の間隙α7)との間に
圧力差が生じにくく、流体は、緩かに多孔機(5)の周
面の多数の小孔(6)を経て圧力差減少板(1119と
の間隙αηに流入し、緩かにこの間隙<1?)を下降し
、下部の流通開口−を経て流出管Q6)に流出するため
、多孔板(5)の外周面のとみ埠は、多孔板(5)の小
孔(6)に吸着されにくいし、またこの多孔板(5)の
小孔(6)に吸着されそうになるごみ等も旋回流によっ
て多孔機(5)から剥ぎとられ、多孔板(5)の目づま
りが自然に解消され、多孔機(5)は常に新鮮な状態に
保たれる。また圧力差減少板餞は、上記のようにして多
孔@ (5)の目づまりを防止する作用があるとともに
、多孔板(5)が内外圧力差によって内側にへこむおそ
れを防止する作用もある。すなわち多孔板(5)は、板
厚を薄くするけど、その小孔(6)内の流体抵抗が少な
くなり、小孔(6)の両側の圧力差も少なくなる1頃向
があり、小孔(6)にごみ等が結まりにくいので、多孔
板(5)の板厚はできるだけ薄くするが、その場合に生
ずる薄い多孔板(5)のへこみの問題を、この圧力差減
少板(1稀によって多孔板(5)の内側間隙aηの圧力
を高めることにより、有効に解消している。
In addition, the above-mentioned relatively light garbage stays on the outer peripheral surface of the perforated plate (5) and moves downward or upward according to the 70% electric charge while rotating and moves to the lower or upper part of the horizontal body (3). This is because there is a cylindrical pressure difference reducing plate 081 which is provided concentrically inside the plate (5) through a gap α force and forms a flow opening between the lower end 01 and the lower part Ql of the perforated plate (5). , this pressure difference reducing plate (18) has the effect of suppressing the flow of fluid trying to pass through the small holes (6) of the perforated plate (5), and the gap between the outer part and the inner part of the perforated plate (5) is α7), and the fluid gently flows into the gap αη with the pressure difference reducing plate (1119) through the many small holes (6) on the circumferential surface of the perforated machine (5). The flow slowly descends through this gap (<1?) and flows through the flow opening at the bottom to the outflow pipe Q6). (6) and is likely to be absorbed by the small holes (6) of this perforated plate (5) are also stripped from the perforated machine (5) by the swirling flow, Clogging is naturally cleared and the perforator (5) is always kept fresh. In addition, the pressure difference reducing plate has the effect of preventing clogging of the porous plate (5) as described above, and also has the effect of preventing the perforated plate (5) from denting inward due to the pressure difference between the inside and outside. In other words, although the perforated plate (5) has a thinner plate thickness, the fluid resistance within the small holes (6) decreases, and the pressure difference on both sides of the small holes (6) also decreases. The thickness of the perforated plate (5) is made as thin as possible to prevent dust from clumping up on the pressure difference reducing plate (1). This can be effectively solved by increasing the pressure in the inner gap aη of the perforated plate (5).

横本体(3)の上部に浮上した軽いごみ等は、★(9)
を取外して、中央開口部(8)より外部に取出すように
する。
Light debris floating on the top of the horizontal body (3) should be removed with ★ (9).
Remove it and take it out from the central opening (8).

次に、3・6図および314図に示す112実施例につ
いて説明する。なお上記第1実施例と同様の部分には同
一の符号を附し、その構造および作用の説明を省略する
Next, the 112th embodiment shown in FIGS. 3 and 6 and 314 will be described. Note that the same parts as in the first embodiment are given the same reference numerals, and the explanation of their structure and operation will be omitted.

横本体(3)は上端開放形であって、多孔板(5)およ
び圧力差減少板QEGの上端を固定支持する円板状の内
蓋(ハ)から4方に支持sC荀を突設し、この4力の支
持部(財)の先端を横本体(3)の内壁面に当接するこ
とによって内蓋(ハ)の横ずれを防止するとともに、多
孔板(5)の上部と槽本体(3)との間を一定の間隔に
保持して、この間に浮上ごみ通口051を設ける。流出
管011ポンプのサクション側に接続する。
The horizontal main body (3) has an open top end, and has support sC protruding from a disc-shaped inner lid (c) that fixedly supports the upper ends of the perforated plate (5) and the pressure difference reducing plate QEG on four sides. By abutting the tip of this four-force support part (goods) against the inner wall surface of the horizontal body (3), the inner lid (c) is prevented from shifting laterally, and the upper part of the perforated plate (5) and the tank body (3) are prevented from shifting laterally. ), and a floating debris port 051 is provided between them. Outflow pipe 011 Connects to the suction side of the pump.

また上記浮上ごみ通口鯵0の上側に位置する液面9句の
レベルにおいて横本体(3)の内側面に突部c70を固
定する。この突部(2′0は、槽本体(3)の上端開口
(2)から液面(ハ)の下方にわたって所定の昧さを有
するとともに、平面的には、槽本体(33)に対する円
帆面部翰と、旋回流に対−5−i傾樹面部1りと、横′
本体(3)の半径方向に一致する下流側面部6υとによ
ってほば6角形状に形成されたものであり、この突部(
ハ)の下流側近傍において横本体(3)に浮上とみ取出
し口C(7!lを設け、この浮上とみ取出しl」04か
ら管−を突設する。
Further, a protrusion c70 is fixed to the inner surface of the horizontal body (3) at the level of the liquid level 9 located above the floating waste port 0. This protrusion (2'0) has a predetermined spacing from the upper end opening (2) of the tank body (3) to below the liquid level (C), and in plan view, it is a round sail with respect to the tank body (33). The side wall, the swirling flow, the -5-i inclined surface section, and the horizontal section.
It is formed into an almost hexagonal shape by the downstream side surface portion 6υ that coincides with the radial direction of the main body (3), and this protrusion (
A floating and sawing outlet C (7!l) is provided in the horizontal body (3) near the downstream side of c), and a pipe is provided protruding from this floating and sawing outlet C (7!1).

そうして、1r3図に示すように、流入管a賜に河川、
池Oa等から引出した管Ct51をフランジ接続し、横
本体(3)内に液を引込み、矛1実施例と同様に液中の
粒子、ごみ等を分離除去する。その際に液よりも比重の
軽いごみ等は、旋回しながら旋回流空間部(4)から浮
上ごみ通口(7!噂を経て液面し四に浮上し、さらにこ
のごみ等は、槽本体(3)の側面に接線方向で接続した
流入管(【場から横本体(3)の内部に流入する液体の
1に回流とともに液面(ハ)で旋回しようとする力瓢上
記突部シ゛0を通過した後は、との突部しηによって相
対的に凹状となった突部((資)の下流側四部(至)に
生ずる渦流に引込まれ【自然に旋回流から分離し、この
下流側に設けられた浮上ごみ取出し口C(3から液面部
分の液とともに自然に外部に排出され、動力を用いるこ
となく1.#上ごみの排出ができる。内蓋(ハ)の下側
部にたまった浮上ごみは、内蓋(ハ)を横本体(3)の
上端開口端より取外して取出す。
Then, as shown in Figure 1r3, the river flows through the inflow pipe a.
A pipe Ct51 drawn out from a pond Oa or the like is connected with a flange, and liquid is drawn into the horizontal body (3), and particles, dirt, etc. in the liquid are separated and removed in the same manner as in the first embodiment. At that time, garbage, etc., which has a specific gravity lighter than the liquid, swirls and floats from the swirling flow space (4) to the floating garbage port (7! (3) The inflow pipe connected tangentially to the side surface of the horizontal body (3) causes the liquid flowing into the interior of the horizontal body (3) to circulate and swirl at the liquid surface (c). After passing through the protrusion, it is drawn into the vortex generated at the four downstream parts of the protrusion, which is relatively concave due to the protrusion η. Floating debris removal port C (3) provided on the side allows the debris to be discharged to the outside along with the liquid at the surface level, allowing for the removal of debris above 1.# without using power. Lower part of the inner lid (C) Remove the floating debris that has accumulated in the container by removing the inner cover (c) from the upper open end of the horizontal body (3).

なお第1図および才2図に示した3・1実施例は、密閉
式のものであり、管流路と管流路との間に設置するのに
適し、液および空気の両方に適用できる。こ第1に対し
、3/6図および314図に示した1適用する。
Embodiment 3.1 shown in Figures 1 and 2 is a closed type, suitable for installation between pipe channels, and applicable to both liquid and air. . 1 shown in Figures 3/6 and 314 is applied to this first example.

〔発明の効果〕〔Effect of the invention〕

才1番目の本発明によれば、円筒形の横本体の内部に旋
回流空間部を介して同心状に円筒形の多孔機を設け、こ
の多孔板の外周面に対応する範囲内で横本体の比較的上
部の0Il1面に接線方向で流入管を接続し、上記多孔
板の下部開口から横本体の比較的下部の側面を経て外部
に流出管な引出したから、流体が横木体内に接線方向か
ら流入する勢いにより、横本体と多孔板との間の旋回流
空間部で旋回流が生じ、比較的重い粒子等は、旋回時に
生ずる遠心力の作用で外側に分離され、横本体の内壁面
に后って1に回しながら下降して底部に沈降し、この市
本体の1氏部の沈降物排出口から外部に排出され、また
比較的軽いごみ等は、多孔板によってl−A過し、この
多孔板の小孔を通過した流体は、の粒子、ごみ等を流体
から有効に分離除去できるとともに、従来のサイクロン
と異なり流出管を流入管よりも下方に設けて圧力ロスを
防ぐ構造となっているため、ηC入管側の圧力が比較的
低圧の場合でも本装置は有効に作用する。また上記比較
的軽いごみ等は、多孔板の外周面に浴つ“(旋回しなが
らその比重に応じて下降または上昇して横本体の下部ま
たは上部に移動するが、多孔板の内側に間隙を介して同
心状に設けられ下端と多孔板の下部との間に流通開口を
形成する円筒形の圧力差減少板があるから、この圧力差
減少板が、多孔板の小孔を勢いよく通過しようと−rる
流体の流れを抑制する作用があり、多孔板の外側部と内
側部の間隙との間に圧力差が生じにくく、流体は、緩か
にの間隙にυiし人し、緩かにこの間隙を下降し、下部
の流通開口を経て流出管に流出するため、多孔板の外周
面のごみ等は、多孔板の小孔に吸着されにくいし、また
この多孔板の小孔に吸着されそうKなるごみ等も旋回流
によって多孔板から剥ぎとられ、多孔板の目詰りが自然
に解消され、多孔板は富に新鮮な状態に保たれる。また
圧力差減少板は、上記のようにして多孔板の目詰りを防
止するのに有効であるとともに、多孔板が内外圧力差に
よって内1lllにへこむおそれを防止している点でも
有効なものである。すなわち多孔板は、板厚を薄くする
ほど、その小孔内の流体抵抗が少なくなり、小孔の両側
の圧力差も少なくなる傾向があり、小孔にごみ等が詰ま
りにくいので、多孔板の板厚はでとるだけ薄くするが、
その場合に生ずる薄い多孔板のへこみの間勉を、この圧
力差減少板によって多孔板の内側の圧力を高めることに
より、有効に解消でき、これは、多孔板を大形化し、取
扱う流体の容匍を増すことを可能にする。
According to the first aspect of the present invention, a cylindrical perforated machine is provided concentrically within a cylindrical horizontal body through a swirling flow space, and the horizontal body is provided within a range corresponding to the outer peripheral surface of the perforated plate. An inflow pipe is connected tangentially to the relatively upper surface of the horizontal body, and an outflow pipe is drawn out from the lower opening of the perforated plate to the outside through the relatively lower side of the horizontal body, so that fluid flows into the crossbody from the tangential direction. Due to the inflowing force, a swirling flow is generated in the swirling flow space between the horizontal body and the perforated plate, and relatively heavy particles are separated to the outside by the action of centrifugal force generated during swirling, and are deposited on the inner wall surface of the horizontal body. Afterwards, it descends while turning to 1 and settles to the bottom, and is discharged to the outside from the sediment discharge port in the 1-degree part of the city body. Relatively light garbage is passed through a perforated plate, The fluid that has passed through the small holes of this perforated plate can effectively separate and remove particles, dirt, etc. from the fluid, and unlike conventional cyclones, the outflow pipe is installed below the inflow pipe to prevent pressure loss. Therefore, this device works effectively even when the pressure on the ηC entry pipe side is relatively low. In addition, the above-mentioned relatively light dust falls on the outer peripheral surface of the perforated plate (while rotating, it descends or rises depending on its specific gravity and moves to the lower or upper part of the horizontal body, but there is no gap inside the perforated plate). Since there is a cylindrical pressure difference reducing plate which is provided concentrically through the hole and forms a flow opening between the lower end and the lower part of the perforated plate, this pressure difference reducing plate will forcefully pass through the small holes of the perforated plate. This has the effect of suppressing the flow of fluid, making it difficult to create a pressure difference between the gap between the outside and inside of the perforated plate, allowing the fluid to slowly flow into the gap and Since it descends through this gap and flows out into the outflow pipe through the flow opening at the bottom, it is difficult for dirt, etc. on the outer surface of the perforated plate to be absorbed by the small holes in the perforated plate; The swirling flow removes the dirt that is likely to be removed from the perforated plate, and the clogging of the perforated plate is naturally eliminated, keeping the perforated plate in a very fresh state. This method is effective in preventing the perforated plate from clogging, and is also effective in preventing the perforated plate from being dented due to the pressure difference between the inside and outside. The thinner the perforated plate is, the lower the fluid resistance within the pore becomes, and the pressure difference on both sides of the pore tends to decrease, making it difficult for the pores to become clogged with dirt, so the perforated plate should be as thin as possible. But,
By increasing the pressure inside the perforated plate using this pressure difference reducing plate, the stress caused by the dents in the thin perforated plate can be effectively eliminated. Enables you to increase your strength.

また12番目の本発明によれば、上記矛1査目の発明と
同一の作用効果が得られる上に、さらに多孔板の上部と
横本体との間に浮上ごみ通口を設け、この浮上ごみ通口
の上側に位置する液面レベルにおいて横本体の内側面に
突部を設け、この突部の下流側近傍において横本体に浮
上とみ取出し口を設けたから、浮上ごみ通口を経て液面
に浮上した軽いごみは、横本体の1il1面に接線方向
で接続した流入管か−ら槽本体の内部に流入する液体の
旋回流とともに液面で旋回しようとするが、上記突部を
通過した後は、この突部によって相対的に凹状となった
突部の下流側に生ずる渦流に引込まれて自然に旋回流か
ら分離し、この下流側に設けられた浮上ごみ取出し口か
ら液面部分の液とともに自然に外部に排出され、動力を
用いることなく浮−hごみのII’出ができる。
Further, according to the twelfth invention, in addition to obtaining the same functions and effects as the first invention, a floating waste port is further provided between the upper part of the perforated plate and the horizontal body, and the floating waste is removed. A protrusion is provided on the inner surface of the horizontal body at the liquid level located above the port, and a flotation and dust removal port is provided in the horizontal body near the downstream side of this protrusion. The floating light debris tries to swirl on the liquid surface with the swirling flow of liquid flowing into the tank body from the inlet pipe connected tangentially to the 1il1 surface of the horizontal body, but after passing the above protrusion, is drawn into the vortex generated on the downstream side of the relatively concave protrusion by this protrusion, and is naturally separated from the swirling flow. Floating garbage can be discharged to the outside naturally without using any power.

【図面の簡単な説明】[Brief explanation of the drawing]

3/1図は本発明のC過装置の第1実施例を示す垂li
!断面図、312図は111図のIt−l線断面図、1
・6図は本発明の)lt2実施例を示す垂直断面図、J
14図はその平面図である。 (1)・・底部、(2)・・沈降物排出口、(3)・・
横本体、(4)・・旋回流空間部、(5)・・多孔板、
(6)・・小孔、QQI・・下h15、aυ・・下部開
口、α四・・流入管、ta61・・流出管、(1′O・
・間隙、(田・・圧力差減少板、(1鐘・・下端、シ嶋
−・流通開口、(ハ)・−浮上ごみ通口、(ホ)・・液
面、Cl1)・・突部、C4カ・・浮上ごみ取出し口。 昭和57年6月25日
Figure 3/1 is a diagram showing the first embodiment of the C filter device of the present invention.
! The cross-sectional view, Figure 312, is the It-l cross-sectional view of Figure 111, 1
・Figure 6 is a vertical sectional view showing the lt2 embodiment of the present invention, J
FIG. 14 is a plan view thereof. (1)...bottom, (2)...sediment discharge port, (3)...
Horizontal body, (4)... swirling flow space, (5)... perforated plate,
(6)...Small hole, QQI...lower h15, aυ...lower opening, α4...inflow pipe, ta61...outflow pipe, (1'O...
・Gap, (field: Pressure difference reduction plate, (1 bell: bottom end, Shijima: circulation opening, (c): floating debris port, (e): liquid level, Cl1): protrusion , C4... Floating garbage outlet. June 25, 1980.

Claims (2)

【特許請求の範囲】[Claims] (1)  底部に沈降物排出口を有する円筒形の横本体
と、この横本体の内部に旋回流空間部を介して同心状に
設けられ周面に多数の小孔を有する円筒形であって下部
を開口した多孔板と、この多孔板の外周面に対応する範
囲内で横本体の比較的上部の11111面に接線方向で
接続した流入管と、上記多孔敗の下部開口から横本体の
比較的下部の側面を経て外部に引出した流出管と、上記
多孔板の内側に間隙を介して同心状に設けられ下端と多
孔板の下f#15との間に流逃開L]を形成する円筒形
の圧力差減少板とを具備したことを特色とするj″I過
装置。
(1) A cylindrical horizontal body having a sediment discharge port at the bottom, and a cylindrical shape having a large number of small holes on the circumferential surface provided concentrically through a swirling flow space inside the horizontal body, Comparison of a perforated plate with an opening at the bottom, an inflow pipe connected tangentially to the relatively upper 11111 plane of the horizontal body within the range corresponding to the outer peripheral surface of the perforated plate, and the horizontal body from the lower opening of the perforated hole. A flow relief opening L] is formed between the outflow pipe drawn out to the outside through the side surface of the lower part of the target and the lower end of the perforated plate, which is provided concentrically with a gap between the inside of the perforated plate and the lower end of the perforated plate. A cylindrical pressure difference reducing plate.
(2)底部に沈降物排出口を有する円筒形の横本体と、
この槽本体の内部に旋回流空間部を介して同心状に設け
られ局面に多数の小孔を有する円筒形であって下部を開
口した多孔板と、この多孔板の外周面に対応する範囲内
で横本体の比較的上部の側面に接線方向で接続した流入
管と、上86多孔板の下部開口から横本体の比較的下部
の側面を経て外部に引出した流出管と、上記多孔板の内
側に間隙を介して同心状に設けられ下端と多孔板の下部
との間に流通開口を形成する円筒形の圧力差減少板とを
具備し、上記多孔板の上部と槽本体との間に浮上ごみ通
口を設け、この浮上ごみ通口の上側に位置する液面レベ
ルにおいて槽本体の内側面に突部を設け、この突部の下
6j6側近傍において横本体に浮上ごみ取出し口を収け
たことす時情とずる1過装置。
(2) a cylindrical horizontal body with a sediment outlet at the bottom;
A cylindrical perforated plate with a large number of small holes on the curved surface and open at the bottom is provided concentrically inside the tank body through a swirling flow space, and within an area corresponding to the outer peripheral surface of the perforated plate. an inflow pipe connected tangentially to the relatively upper side surface of the horizontal body, an outflow pipe led out from the lower opening of the upper perforated plate through the relatively lower side surface of the horizontal body, and the inside of the perforated plate. and a cylindrical pressure difference reducing plate provided concentrically with a gap therebetween and forming a flow opening between the lower end and the lower part of the perforated plate, floating between the upper part of the perforated plate and the tank body. A garbage port is provided, a protrusion is provided on the inner surface of the tank body at the liquid level located above the floating garbage port, and a floating garbage removal port is placed in the horizontal body near the bottom of this protrusion on the 6j6 side. This year's current situation and one passing device.
JP57109544A 1982-06-25 1982-06-25 filtration device Expired JPS6015372B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57109544A JPS6015372B2 (en) 1982-06-25 1982-06-25 filtration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57109544A JPS6015372B2 (en) 1982-06-25 1982-06-25 filtration device

Publications (2)

Publication Number Publication Date
JPS59310A true JPS59310A (en) 1984-01-05
JPS6015372B2 JPS6015372B2 (en) 1985-04-19

Family

ID=14512936

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57109544A Expired JPS6015372B2 (en) 1982-06-25 1982-06-25 filtration device

Country Status (1)

Country Link
JP (1) JPS6015372B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20010038247A (en) * 1999-10-22 2001-05-15 황종균 Filtering apparatus
GB2367774A (en) * 2000-07-06 2002-04-17 John Herbert North Multiple cyclone separation unit

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61180072U (en) * 1985-04-27 1986-11-10

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20010038247A (en) * 1999-10-22 2001-05-15 황종균 Filtering apparatus
GB2367774A (en) * 2000-07-06 2002-04-17 John Herbert North Multiple cyclone separation unit
GB2367774B (en) * 2000-07-06 2004-04-28 John Herbert North Improved air/particle separator

Also Published As

Publication number Publication date
JPS6015372B2 (en) 1985-04-19

Similar Documents

Publication Publication Date Title
CA1074237A (en) Baffle and wash trough assembly for granular-media filters
KR100715286B1 (en) Whirl type separator with filter
JP2009154051A (en) Simple filtration apparatus
JPS58156314A (en) Filter apparatus
CN205516881U (en) Strengthen superposed layer spiral vertical flow settling pond
JPS59310A (en) Filter apparatus
CN110002620A (en) Spiral-flow filter
JPS58189008A (en) Apparatus for removing turbidity of water
KR102222553B1 (en) Filtration device to remove contaminants by rotating the contaminated fluid
CN210108814U (en) Hierarchical formula water sample preprocessing device
JPH06312111A (en) Filtration machine
JPH0299106A (en) Solid-liquid separator
JP4277589B2 (en) Upflow filter
WO1990011813A1 (en) Liquid processing apparatus, its continuous liquid processing apparatus and its continuous liquid processing method
JP6542746B2 (en) Solid-liquid separation processor
CN208327569U (en) A kind of new type sewage purifier
KR102511322B1 (en) Floating backwash filter device for pretreatment of high concentration water
KR20010038247A (en) Filtering apparatus
US4798677A (en) Filterator for separator
KR0138580B1 (en) Filtering method of floating material and apparatus using the same
RU207906U1 (en) INERTIAL-GRAVITATIONAL MUD FILTER WITH TANGENTIAL WATER SUPPLY
KR20190059479A (en) Settling tank using vortex
KR102260152B1 (en) Cyclone type disk filter
JPS5834019A (en) Strainer
JPS643453Y2 (en)