JPS621415A - Sand filter apparatus - Google Patents

Sand filter apparatus

Info

Publication number
JPS621415A
JPS621415A JP60137342A JP13734285A JPS621415A JP S621415 A JPS621415 A JP S621415A JP 60137342 A JP60137342 A JP 60137342A JP 13734285 A JP13734285 A JP 13734285A JP S621415 A JPS621415 A JP S621415A
Authority
JP
Japan
Prior art keywords
chamber
sand
water
pipe
filter
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
JP60137342A
Other languages
Japanese (ja)
Other versions
JPH06164B2 (en
Inventor
Shigeru Uchida
繁 内田
Katsumi Iwasaki
岩崎 克己
Katsuya Kobayashi
小林 勝弥
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.)
Proterial Ltd
Original Assignee
Hitachi Metals Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Metals Ltd filed Critical Hitachi Metals Ltd
Priority to JP60137342A priority Critical patent/JPH06164B2/en
Publication of JPS621415A publication Critical patent/JPS621415A/en
Publication of JPH06164B2 publication Critical patent/JPH06164B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Filtration Of Liquid (AREA)

Abstract

PURPOSE:To enhance the separation effect of the suspended substance adhered to filter sand, by mounting a conical deflector to the upper end of the rising pipe at the center of a sand filter apparatus for permitting the passage of raw water to a horizontal direction and receiving the same in a revolving tank having a conical shape throttled at the lower part thereof. CONSTITUTION:Raw water enters a raw water chamber 30 from a supply port 14 and further passes through a filter chamber 31 wherein coarse filter sand is arranged in the side of an outer support wall 2 and fine filter sand in the side of an inner support wall 3 and, at this time, the suspended substance of raw water is collected in a size order. Clarified water reaches a water collection chamber 32 and subsequently fallen through the water collection chamber 32 to take a U-turn to be flowed to a drain chamber 34 and a drain port 15. A slight amount of filter sand is accumulated in a sedimentation cylinder 6 while the filter sand 31 in the filter chamber 31 is tumbled on the bottom 51 thereof to rise through a rising pipe 8 and discharged in a revolving tank 9 through a conical deflector. A revolving stream is generated in the revolving tank 9 by emitted water and sand is fallen downwardly to be tumbled on an upper chute 10 and reaches the filter chamber 31.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は液体を砂ろ過層中水平方向に通過させて清澄に
ろ過する装置の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to an improvement in a device for filtering a liquid horizontally through a sand filter layer to obtain clear filtration.

〔従来の技術〕[Conventional technology]

砂ろ過して清澄水を得る手段として、特許第155.7
56号に開示があシ近年では、特公昭48−20070
号とか特公昭51−34587号が代表例としてちる。
As a means of obtaining clear water through sand filtration, Patent No. 155.7
The disclosure is in No. 56, but in recent years, it has been disclosed in
A typical example is Special Publication No. 51-34587.

これらに共通していえることは次のとおシである。What these all have in common is the following.

■ 槽内に外壁と内壁と内壁内に集水室とを同心に設け
て外壁と内壁の間隔にろ過r!pを充填して汚染水が輻
流する。
■ An outer wall, an inner wall, and a water collection chamber inside the inner wall are installed concentrically in the tank, and filtration is carried out between the outer wall and the inner wall! Contaminated water flows through the tank.

■ 充填したろ過砂は下降して、水圧ま九はエヤーによ
って集水室内の管路内を上昇し、ろ過砂層のろ過砂が下
降移動する。
■ The filled filter sand descends, the water pressure rises in the pipe inside the water collection chamber using air, and the filter sand in the filter sand layer moves downward.

■ 外壁と内壁には開口部を設けて汚染水と清澄水は通
過するがろ過砂層を形成しているろ過砂を支持している
■ Openings are provided in the outer and inner walls to allow contaminated water and clear water to pass through, but to support the filter sand that forms the filter sand layer.

■ 管路内金上昇し几ろ過砂は管路出口下のシュートを
転がるか、ま穴は直接的にろ過砂層O上表面に水中沈降
する。ろ過砂の転動作用によって、粗粒と細粒の分布に
別れるような傾向が発生する。
■ The gold in the pipe rises and the filtered sand rolls down the chute below the pipe outlet, or directly sinks into the water on the upper surface of the filtered sand layer O through holes. Due to the rolling action of the filter sand, there is a tendency for the distribution to be divided into coarse grains and fine grains.

■ ろ過砂に捕捉され九懸濁物(大・小の混入物を含め
て)は水表面から系外へ除去する。特に整流効果をも九
せる節回状の越流樋を設けているのもおる。
■ The suspended solids (including large and small contaminants) captured by the filter sand are removed from the water surface and out of the system. In particular, some have a gutter-shaped overflow gutter that also improves the rectification effect.

これらの説明によって次のことが理解できる。From these explanations, the following can be understood.

ろ過砂層を横断する通水によって砂層が懸濁物を捕捉し
て清澄水を得ることができる。砂を循環して移動する間
に懸濁物を砂から分離させて除去するという操作を成し
ている。
By passing water across the filter sand layer, the sand layer traps suspended matter and clear water can be obtained. This operation involves separating suspended matter from the sand and removing it while the sand is being circulated.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

これらの砂ろ過装置は幾つ、かの技術的欠点があって、
よシ高度な清澄水が得られなかっ几、すなわち、ろ過砂
と懸濁物との分離効果がよくなかったのでおる。
These sand filters have several technical drawbacks.
This is because highly clear water could not be obtained, that is, the separation effect between filter sand and suspended matter was not good.

ま九、ろ過砂の返送においては系外からの水を使用する
かエヤ装置が必要であり、コンパクト・簡易操作という
条件を溝穴していない。
Furthermore, returning the filter sand requires the use of water from outside the system or an air system, which does not meet the requirements of compact size and easy operation.

q!tVc blowlng Alrの場合には細気泡
がろ過砂に付着するのでろ過砂の沈降、転勤を阻害する
し、浮遊するので°懸濁物を含んだ水と共に逸失するこ
とが発生する。そして、汚染水を供給する水量とか圧力
の変動によって楕円の水表面が変位するし、初期・終期
の運転に際しては清澄水にろ過砂が混入し7tシ、乾燥
砂でおるが故に仝気が接触していることから気泡が砂に
付着し次状態となり逸流することもあり九。
q! In the case of tVc blowing Alr, fine bubbles adhere to the filter sand, which inhibits the settling and transfer of the filter sand, and because they float, they are lost together with the water containing suspended matter. The elliptical water surface is displaced due to fluctuations in the amount and pressure of contaminated water being supplied, and during the initial and final stages of operation, 7 tons of filtered sand is mixed into the clear water, and because it is dry sand, air comes into contact with it. Because of this, air bubbles may adhere to the sand and cause the following state to occur and the flow to flow away.

したがって、本発明の目的はコンパクトな礪造で、簡易
操作によって高度な清澄水を安価に得られる砂ろ過装置
を提供することにある。
Therefore, an object of the present invention is to provide a sand filtration device that is compact in construction and that can obtain highly clear water at low cost through simple operation.

更に目的とするところは、砂の逸失をなくし、砂を循環
する水質を選ばずに有効な清澄水を多く得て多用途に適
する砂ろ過装置全提供することにある。
A further object is to provide a sand filtration device that eliminates loss of sand, obtains a large amount of effective clear water regardless of the quality of the water that circulates the sand, and is suitable for a variety of uses.

〔問題点を解決するための手段〕[Means for solving problems]

この目的を達成する几めに原水の流入量を適切にし、旋
回流によってろ過砂を強制的に洗浄分離するようにし、
水表面に浮遊するスカムを適切に除去することを特徴と
する。この几め、筒状外壁の下方t・ゾ、ウゴ状に絞っ
几タンクゴディ内に通水可能な外支持壁と内支持壁を設
け、これらの壁間にろ過砂を充填する。内支持壁の内方
には同心に3重の管を設けて、タンクボディ側から原水
室、ろ過室、集水室、排出室、滞留室と上昇管を構成す
る。上昇管内の水tエヤリフトによって、タンクボディ
内の上域にある上室の旋回タンク中央に導き入れること
によって充填したろ過砂も同時に供給される・−万、ポ
ンプによって上室から水を抜きとって旋回タンクに旋回
流が発生するように供給するとろ過砂と懸濁物とが分離
する。ろ過砂は再びろ過室に上シユートを転動して沈積
するし。
In order to achieve this purpose, the amount of raw water inflow is adjusted appropriately, and the filter sand is forcibly washed and separated by swirling flow.
It is characterized by appropriately removing scum floating on the water surface. An outer support wall and an inner support wall through which water can pass are provided in the tank body below the cylindrical outer wall, and filter sand is filled between these walls. Three concentric pipes are installed inside the inner support wall to form a raw water chamber, a filtration chamber, a water collection chamber, a discharge chamber, a retention chamber, and a rising pipe from the tank body side. Water in the rising pipe is introduced into the center of the swirling tank in the upper chamber in the upper area of the tank body by the air lift, and the filter sand filled in is also supplied at the same time. When supplied to the swirling tank so as to generate a swirling flow, filter sand and suspended matter are separated. The filter sand is deposited again by rolling the upper chute into the filter chamber.

懸濁物は高濃度の汚濁水となってタンクデディ外へ吐出
する。上室での水表面に浮遊するスカムは上下動自在な
ファネルに流入し前記汚濁水と共にタンクデディ外へ吐
出する。
The suspended solids become highly concentrated polluted water and are discharged outside the tank. The scum floating on the water surface in the upper chamber flows into a vertically movable funnel and is discharged out of the tank along with the polluted water.

タンクボディには更に原水室と連通する溢流管を設けて
外支持壁を通過する原水の量を一定にし、内支持壁の下
方には砂の沈澱室を設けてドレンで排出する。これらを
具備して清澄水を得る装置であるO 〔災施例〕 第1図〜第3図を以て本発明の外観を簡単に説明する。
The tank body is further provided with an overflow pipe that communicates with the raw water chamber to keep the amount of raw water passing through the outer supporting wall constant, and a sand settling chamber is provided below the inner supporting wall to drain the sand. [Example] The appearance of the present invention will be briefly explained with reference to Figs. 1 to 3.

タンクボディ1に安全枠37付のハシゴ38を固着して
設け、サポート39を介して床40に固定する。
A ladder 38 with a safety frame 37 is fixed to the tank body 1 and fixed to the floor 40 via a support 39.

タンクボディ1の上方には手摺41を設けてハシゴ38
を登って点検とか保守が安全にできるようにし、集水マ
ス42と溢流口29を設け、中程にには排出口15、吐
出口16、吸引口43.吐出口44、エヤ供給口19t
−設ける。タンクボディ1の下方には、汚染されて懸濁
物を多く含む原水の供給口14、゛ドレン管17及び給
水と砂の排出を兼用するノズル45を設ける。
A handrail 41 is provided above the tank body 1 and a ladder 38 is provided.
A water collection mass 42 and an overflow port 29 are provided, and a discharge port 15, a discharge port 16, a suction port 43. Discharge port 44, air supply port 19t
- Provide. Below the tank body 1, there are provided a supply port 14 for raw water that is contaminated and contains a lot of suspended matter, a drain pipe 17, and a nozzle 45 that serves both for water supply and sand discharge.

第4図に本発明の概略構成を示し、第5〜14図でその
詳細な構成について説明する。
FIG. 4 shows a schematic configuration of the present invention, and the detailed configuration will be explained in FIGS. 5 to 14.

第4図において、タンクボディ1は垂立する筒状で円筒
または多角形筒でもよく、タンクメrイ1内に外支持壁
2と内支持壁3と集水筒5と上昇管8及び沈澱筒6を略
同心に設ける。内支持壁3の下方には沈IIRfrJ6
と下シ、−)1設はサポート4などで適宜にタンクボデ
ィ1へ固定し、沈澱筒6と連通したドレン管17をタン
クMfイ1外へ導き弁18を設ける。
In FIG. 4, the tank body 1 has a vertical cylindrical shape, and may be a cylindrical or polygonal cylinder. are provided approximately concentrically. Below the inner support wall 3 is a sink IIRfrJ6.
and lower, -) one is appropriately fixed to the tank body 1 with a support 4 or the like, and a drain pipe 17 communicating with the sedimentation cylinder 6 is led out of the tank Mf1 and a valve 18 is provided.

上昇管8と集水筒5の間には隔筒46を設けて、隔@4
6の周辺に排出室34を形成し、タンクボディ1と外支
持壁2が成す空間を原水皇30とし、外支持壁2ど内支
持壁3がなす空間をろ過室31としてろ材でおるろ過砂
13を充填する。同じく、内支持壁3と集水筒5がなす
空間金集水室32とし、集水筒5と隔筒46が成す空間
を排出室34とし、隔筒46と上昇管8とが成す空間は
滞留室47とする。
A separation pipe 46 is provided between the rising pipe 8 and the water collection pipe 5, and the partition @4
A discharge chamber 34 is formed around the tank body 1 and the outer support wall 2, the space formed by the tank body 1 and the outer support wall 2 is defined as the Gensuiko 30, and the space formed by the outer support wall 2 and the inner support wall 3 is defined as the filtration chamber 31, and the filter sand is filtered with a filter medium. Fill 13. Similarly, the space formed by the inner support wall 3 and the water collection tube 5 is called a water collection chamber 32, the space formed by the water collection tube 5 and the partition tube 46 is called a discharge chamber 34, and the space formed by the partition tube 46 and the rising pipe 8 is called a retention chamber. 47.

隔筒46の上方には上シュー)10と旋回タンク9t″
設けて吐出口44と吐出管27と流量計23と弁21と
逆止弁22をポンプ20に連通して設ける。
Above the partition 46 are an upper shoe) 10 and a rotating tank 9t''.
A discharge port 44, a discharge pipe 27, a flow meter 23, a valve 21, and a check valve 22 are provided in communication with the pump 20.

旋回タンク9の一方には吐出管48を介して吐出口に連
通して設け、吐出管48路の途中に伸縮管121c介し
て7アネル1lt一連通して設げる。
One side of the swirling tank 9 is provided in communication with a discharge port via a discharge pipe 48, and a 7-anel 1lt is provided in the middle of the discharge pipe 48 in series via a telescopic pipe 121c.

タンクボディ1の中心下辺から旋回タンク9の中心に向
けて設は窺上昇管8の下辺にはエア室50を設け、エヤ
供給口19とエア室50ft連通する管路49を配する
An air chamber 50 is provided at the lower side of the rising pipe 8 extending from the center lower side of the tank body 1 toward the center of the rotating tank 9, and a conduit 49 communicating with the air supply port 19 through 50 feet of the air chamber is arranged.

前記した弁21と連通して弁24と流量計25を給水管
28に設けてノズル45に結合し、ポンプ20と上昇管
8下端及びろ過室31とは連通するようにする。
A valve 24 and a flow meter 25 are provided in the water supply pipe 28 in communication with the above-mentioned valve 21 and connected to the nozzle 45, so that the pump 20 and the lower end of the riser pipe 8 and the filtration chamber 31 are communicated with each other.

タンクボディ1内は上から上室36、ろ過室31、下室
35の順に配置し、タンクボディ1の下面は中心に向っ
て絞った7アネル状の底51とする。
Inside the tank body 1, an upper chamber 36, a filtration chamber 31, and a lower chamber 35 are arranged in this order from the top, and the lower surface of the tank body 1 has a bottom 51 in the form of a seven-annel shape narrowing toward the center.

次に第5図に基づいて本発8A′s成の上室36部につ
いて説明する。
Next, the upper chamber 36 section of the 8A's structure of the present invention will be explained based on FIG.

旋回タンク9の外郭は上部が円筒52で下部がジョウゴ
状下絞シのコーン53で、外郭の内方に旋回タンク9と
同心で傘54とシュート55と集水筒56を設ける。
The outer shell of the rotating tank 9 has a cylinder 52 at the top and a funnel-shaped cone 53 at the lower part, and an umbrella 54, a chute 55, and a water collecting tube 56 are provided inside the outer shell concentrically with the rotating tank 9.

上昇管8はコーン53と集水筒56とシュート55を貫
通して設け、コーン53の最下部の大径は゛上昇管8の
行径より大きくして間隙58を設ける。
The rising pipe 8 is provided to pass through the cone 53, the water collecting pipe 56, and the chute 55, and the diameter of the lowermost part of the cone 53 is made larger than the row diameter of the rising pipe 8 to provide a gap 58.

上昇管8の上端吐出部57Fi傘54の下方で吐出水が
拡がって吐出するようにし、傘54とシュート55の間
から周辺の万へよシ砂粒子が流出し易い構成とする。
The discharge water is spread and discharged below the upper end discharge part 57Fi of the riser pipe 8 and the umbrella 54, and the structure is such that the sand particles easily flow out from between the umbrella 54 and the chute 55 to the surrounding area.

円筒52の内壁接線方向に吐出管27の吐出口591開
口する。
A discharge port 591 of the discharge pipe 27 opens in the tangential direction of the inner wall of the cylinder 52 .

一方、排出管60は集水筒56と円筒52を貫通して吐
出管48に結合し、さらに吐出管48はタンクボディ1
を貫通して吐出口16と連通して設ける。
On the other hand, the discharge pipe 60 passes through the water collecting pipe 56 and the cylinder 52 and is connected to the discharge pipe 48.
The discharge port 16 is provided so as to penetrate through the discharge port 16 and communicate with the discharge port 16.

尚、排出管60にfi常に大気へ開口する管84ヲ8.
ケてサイホンブレーカとし、吐出口59は下方へ向けて
3〜10度の角度で吐出するようにする。
Note that the exhaust pipe 60 is equipped with a pipe 84 which is always open to the atmosphere.
A siphon breaker is used, and the discharge port 59 is configured to discharge downward at an angle of 3 to 10 degrees.

タンクボディ1の上室36には前記した旋回タンク9と
7アネル11t−設げることを明らかにし友がファネル
11について次に述べる。
The upper chamber 36 of the tank body 1 is provided with the above-mentioned swirl tank 9 and seven annels 11t, and the funnel 11 will be described next.

原水呈30へはポンプによるか自然流下によるかまたは
それらの兼用をして原水を流入させる。
Raw water is introduced into the raw water source 30 by a pump, by gravity flow, or by a combination of these methods.

すると上室36部に水面A61が形成され、ろ過操作の
運転を開始するとスカムが水面人の表層近くに浮遊する
。このスカムを効率よく表層に追随して除去する丸めに
ファネル11を設け、ファネル11はタンクボディ1に
固着し九ブラケット62にスピンドル63とナツト64
で位置調整可能に固定される。
Then, a water surface A61 is formed in the upper chamber 36, and when the filtration operation is started, scum floats near the surface layer of the water surface. A round funnel 11 is provided to efficiently follow and remove this scum from the surface layer.
The position can be adjusted and fixed.

7アネル11と吐出管48は伸縮管12を介して連通し
ているので、スビ/ドル63の上下動によってファネル
11は自由に水面A61に追随することができる。
Since the annel 11 and the discharge pipe 48 communicate with each other via the telescopic pipe 12, the funnel 11 can freely follow the water surface A61 by vertical movement of the slot/dol 63.

一方、原水室30と連通ずる全流管65i設げて集水マ
ス42内に噴出口120を設け、水面人61からせき板
66’tオーバーフローして水面B67i形成するよう
にする。せき板66には水面^61のレベルを調整しつ
\整流する機finもたせることは云うまでもないが、
集水マス42では王室36の茨層水と原水の余剰水が合
わさって水面B67t−形成し、溢流口29に集まり、
他へと流水するようにする。
On the other hand, a full flow pipe 65i communicating with the raw water chamber 30 is provided and a spout 120 is provided in the water collection mass 42 so that the weir plate 66't overflows from the water surface person 61 to form a water surface B67i. It goes without saying that the weir plate 66 is equipped with fins that adjust the level of the water surface ^61 and rectify the flow.
In the water collection mass 42, the thorn layer water of the royal house 36 and the surplus water of the raw water are combined to form a water surface B67t-, which collects at the overflow port 29.
Allow water to flow elsewhere.

尚、タンク〆ディ1に旋回タンク9+吐出管48とかフ
ァネル11を固着しても取外し易いように種々の考慮を
払っている。
In addition, various considerations have been made so that even if the rotating tank 9 + discharge pipe 48 or the funnel 11 are fixed to the tank closing day 1, they can be easily removed.

それは、7−yンジA68とかフランツB69、ネジ継
手人70.ネジ継手B71などであり、特にフランツ人
68はタンク〆デイ1に管座を固着しておいてパツキン
を介して吐出口16の管に固着のフランツをネジで締結
するようにしているので1組立てと保修分解が容易な手
段全構築している。
It is 7-yen A68, Franz B69, screw jointer 70. This is a threaded joint B71, etc., and in particular, the Franz 68 fixes the pipe seat on the tank closing day 1, and then fastens the fixed Franz to the pipe of the discharge port 16 with a screw through a gasket, so it requires only one assembly. And the entire structure is easy to disassemble and maintain.

第6〜第9図に基づいてろ過室310周辺構成を更に詳
細に述べる。
The configuration around the filtration chamber 310 will be described in more detail based on FIGS. 6 to 9.

原水のフローはWa = Wgの矢印で表し、ろ送砂の
流れはS&〜S・の矢印で表わし、水とろ送砂の混った
流れ金W−と表わしている。このフローは構成と共に後
述する。
The flow of raw water is represented by the arrow Wa=Wg, the flow of the filtered sand is represented by the arrows S&~S., and the flow of water and the filtered sand is represented by the mixed flow W-. This flow will be described later together with the configuration.

外支持壁2は下見板72と孔73で構成した第7.8図
に示すようなパーツを複数個設ける。円弧状ま九は折板
状の断面をし九下見板72はろ過室31側に設け、下端
77と接する水平線76からα1なる仰角線75よシ上
万に孔73を設ける。
The outer support wall 2 is provided with a plurality of parts as shown in FIG. 7.8, each consisting of a clapboard 72 and a hole 73. The arcuate plate 72 has a folded plate-like cross section, and the plate 72 is provided on the filtration chamber 31 side, and a hole 73 is provided above the elevation line 75 of α1 from the horizontal line 76 in contact with the lower end 77.

α1はろ送砂の形状・質とか下端77からの吐出水流速
、圧力などくよって一定ではないが、約25〜45度で
ある。孔73を通過し友原水は滞留174t−経て下見
板72に沿って下端77に至り、この周辺からろ過室3
1へと流入する。
α1 is not constant depending on the shape and quality of the filtered sand, the flow rate of water discharged from the lower end 77, the pressure, etc., but is approximately 25 to 45 degrees. The Tomohara water passes through the hole 73 and accumulates for 174 tons, reaches the lower end 77 along the clapboard 72, and flows from this area into the filtration chamber 3.
1.

第9図に内支持壁3部分の断面を示す。FIG. 9 shows a cross section of the inner support wall 3 portion.

ろ過室31には内方へ行くに従って細粒となるようにろ
送砂13が充填され、内支持壁3で集水室32と隔てる
が、細粒のろ送砂13は内支持壁3全通過しないが水の
みが通過する構成が希ましい。本発明では第9図金−実
施例として、外面78の空隙80を小さくし内面79の
空隙81を大きくした個々の断面が略三角形をし九パー
スクリーン状のものを例示する。この場合、空隙80を
小さくすればするほどろ送砂13が細粒でも通過しない
し、空隙80と空隙81の間隔は斬増するのでろ送砂1
3が詰らない。
The filtration chamber 31 is filled with filter sand 13 that becomes finer as it goes inward, and is separated from the water collection chamber 32 by the inner support wall 3. A configuration that does not allow water to pass through, but allows only water to pass through, is rare. In the present invention, as an example shown in FIG. 9, a structure having a substantially triangular cross-section and a nine-percent screen shape is illustrated in which the void 80 on the outer surface 78 is made smaller and the void 81 on the inner surface 79 is enlarged. In this case, as the gap 80 is made smaller, the filter sand 13 will not pass through even fine grains, and the distance between the gap 80 and the gap 81 will be drastically increased.
3 doesn't get stuck.

他の例としては、多孔質のセラミックで内支持壁3を形
成してもよいし、また活性炭などより細孔を有して水の
連通する物質を用いるとろ過の効果が挙る。特に外面7
8の空隙80にはろ送砂13の詰り、ブリッジが水圧と
ろ送砂土圧によって発生し易く、二次スクリーンを形成
する。この詰りとブリッジ現象によって更に懸濁物がこ
こに捕捉されて三次スクリーンを形成すると原水の処理
量がダウンする。原水質とか砂質によってこのような現
象が発生するので、内支持壁3に七−タによる振動とか
超音波などによる微振動を付加すると二次スクリーン、
三次スクリーンを回避することができる。図示はしない
がこれらを以て構成すると更に効果がアッグする。
As another example, the inner support wall 3 may be formed of porous ceramic, or a material with pores that communicate with water, such as activated carbon, may be used for better filtration effects. Especially the outer surface 7
The gaps 80 of 8 are likely to be clogged with the filter sand 13 and bridges are likely to occur due to the water pressure and the soil pressure of the filter sand, forming a secondary screen. Due to this clogging and bridging phenomenon, suspended solids are further trapped here and form a tertiary screen, reducing the throughput of raw water. This phenomenon occurs depending on the quality of the raw water or sand, so if you apply vibrations from a hexameter or ultrasonic waves to the inner support wall 3, it will cause a secondary screen,
Tertiary screens can be avoided. Although not shown in the drawings, if these are included, the effect will be further enhanced.

第10図は旋回タンク9への吐出水を得る部分の詳細図
で、タンクゲディ1を貫通して、吸引管26i上室36
に臨ませて設け、先端にラッパ状の吸入口82を固着す
る。
FIG. 10 is a detailed view of the part that obtains discharged water to the swirling tank 9.
A trumpet-shaped suction port 82 is fixed to the tip.

上室36の水表面近く1′i懸濁物が多く浮遊している
し、上室の下辺ではろ送砂13が沈降する域でおるので
、吸引口8211この沈降域の直上辺がペストである。
There are many suspended substances floating near the water surface of the upper chamber 36, and the lower part of the upper chamber is the area where the filtered sand 13 settles, so the area directly above this settling area of the suction port 8211 is pest. be.

この位置に吸入口82の開口83を臨ませて吸引管26
と迷通し、水を集水してポンプ20で圧送するのである
With the opening 83 of the suction port 82 facing this position, the suction pipe 26
The water is collected and pumped by the pump 20.

吸引管26の固定は、前述したようにフランジ人68と
同等の方法を用いる。
The suction tube 26 is fixed using the same method as the flange member 68, as described above.

第11図に基づいて、タンク〆ディ1の下室35付近を
詳述する。
Based on FIG. 11, the vicinity of the lower chamber 35 of the tank closing day 1 will be described in detail.

ろ過室31の下方に下部が9のi状の下シ一一)7t−
設けその上端は内支持壁3の下方に設は九沈澱筒6に接
しないように空隙85をもたせ、その下端は底51に接
しないように空1!1i86に設ける。沈澱筒6の下部
は微細なろ送砂13が貯るように内方へ絞っ九底87を
設ゆて隔筒46に固定し下室35と流通しないようにす
る。
Below the filtration chamber 31, there is an i-shaped bottom with a bottom part of 9.
A gap 85 is provided at the upper end of the inner support wall 3 so as not to contact the sedimentation cylinder 6, and a gap 85 is provided at the lower end thereof so as not to contact the bottom 51. The lower part of the sedimentation cylinder 6 is narrowed inward so that the fine filtered sand 13 can be stored therein, and nine bottoms 87 are provided and fixed to the partition cylinder 46 to prevent communication with the lower chamber 35.

上昇管8は渦管46の内方に設け、上昇管8を取除いて
も排出室34の水質が変らないようにするための滞留室
47を設ける。
The riser pipe 8 is provided inside the vortex pipe 46, and a retention chamber 47 is provided to prevent the water quality in the discharge chamber 34 from changing even if the riser pipe 8 is removed.

上昇管8外部にエア室50t−設けてエヤの管路49と
連通し、エヤ室50と上昇管8内を連通する細孔88t
−複数個設けて均等な圧力と流量のエヤが細孔88全通
って上昇管8内に通気可能にする。
An air chamber 50t is provided outside the riser pipe 8 and communicates with the air conduit 49, and a pore 88t communicates between the air chamber 50 and the inside of the riser pipe 8.
- By providing a plurality of holes, air with equal pressure and flow rate can pass through all the holes 88 and ventilate into the riser pipe 8.

ポンプ20と連通の給水管28は底51の最下部で中心
位置にフランジ89を設けて吐出口90に臨ませて、水
が堆積ろ送砂92を浮揚するようにする。
A water supply pipe 28 communicating with the pump 20 is provided with a flange 89 at the center at the lowest part of the bottom 51 so as to face the discharge port 90 so that the water floats the sand 92 accumulated therein.

第12図は原水の供給付近金示し、第13図は第12図
のタンク2デイ1中心に対して反対側付近を示す。
FIG. 12 shows the raw water supply area, and FIG. 13 shows the area opposite to the center of tank 2 and day 1 in FIG. 12.

タンク2デイ1に原水の供給口14を設けて原水室30
に原水が入るようにする。タンク2デイ1の内面93と
ほぼ平行で一周する胴板95に設けて円板94でこれら
の間を継ぎ固定する。こうして円筒状の空間96が形成
される。空間96の下端′97は原水室30へ開放とす
るが、供給口14付近にのみ円弧板98を設けて、孔7
3への直流全回避し、対向する位置99にまで均等流と
なるようにする。
A raw water supply port 14 is provided in the tank 2 day 1 and the raw water chamber 30 is installed.
Allow raw water to enter. It is provided on a body plate 95 that is approximately parallel to the inner surface 93 of the tank 2-day 1 and goes around once, and a disk 94 is used to connect and fix the space between them. In this way, a cylindrical space 96 is formed. The lower end '97 of the space 96 is open to the raw water chamber 30, but an arcuate plate 98 is provided only near the supply port 14 to close the hole 7.
Direct current to the position 99 is completely avoided, and a uniform flow is made even to the opposing position 99.

尚、空間96は供給口14から対向する位置99に行く
に従って空間96の断面積が新派するようにすると原水
室30内に均一の圧力・流速となる。tた、空間96の
下部の円弧板98を一周するようにし、孔の個数tfc
は孔径を選択しても同等の効果がある。
If the cross-sectional area of the space 96 increases as it goes from the supply port 14 to the opposing position 99, a uniform pressure and flow rate will be achieved in the raw water chamber 30. In addition, the circular arc plate 98 at the bottom of the space 96 is made to go around once, and the number of holes tfc
The same effect can be obtained by selecting the pore size.

第5図〜第13図に基づいて、水と懸濁物とろ送砂の動
き全説明する。
The movements of water, suspended matter, and filtered sand will be fully explained based on FIGS. 5 to 13.

懸濁物を含んで汚染している原水は供給口14から空間
96に入シ込み、下端97から原水室30へ均等な流量
・圧力で充満する。
The raw water contaminated with suspended matter enters the space 96 from the supply port 14 and fills the raw water chamber 30 from the lower end 97 with uniform flow rate and pressure.

外支持壁2の孔73を通過した原水は下見板72で下向
流になるように整流され、充填されているろ送砂13は
仰角線75に安息角として保持される。
The raw water that has passed through the holes 73 in the outer support wall 2 is rectified by the clapboard 72 so that it flows downward, and the filled filter sand 13 is held at the angle of repose at the elevation line 75.

外支持壁21!Aにより大きなろ送砂が配置され、内支
持壁3側により小さなろ送砂が配置されているので、こ
れらの大空隙を通って小空隙へと至る間に、原水の懸濁
物は大きさの順に捕捉される。
Outer support wall 21! Larger filter sand is placed on the side A, and smaller filter sand is placed on the inner support wall 3 side, so that while passing through these large gaps and reaching the small gaps, the suspended matter in the raw water decreases in size. are captured in this order.

第6図に示した矢印Wa + wb、 I We +の
動きをし、懸濁物を除去し几清澄水は内支持壁3の空隙
80゜81を通って集水室32に至る。矢印WdとW・
の動きをする。
The suspension moves as indicated by the arrows Wa+wb and IWe+ shown in FIG. 6, and the suspended matter is removed, and the clear water passes through the gap 80.degree. 81 of the inner support wall 3 and reaches the water collection chamber 32. Arrows Wd and W・
make a movement.

次に第11図に基いて清澄水とろ送砂13の動きを説明
する。
Next, the movement of the clear water and the filtered sand 13 will be explained based on FIG.

集水132i下降して矢印Wfに至シ、沈澱@6内でU
ターンして排出室34に至る。矢印Wgに示す。そして
、第6図に示す矢印whから排出口15へ至る矢印W1
の方向へ清澄水は流れる。
Collected water 132i descends to arrow Wf, U in sedimentation @ 6
Turn and reach the discharge chamber 34. It is shown by arrow Wg. Then, an arrow W1 leading from the arrow wh shown in FIG. 6 to the discharge port 15
Clear water flows in the direction of.

内支持壁3を清澄水と共に若干量のろ送砂が通過するの
で、この砂は沈澱筒6内に沈澱砂91として堆積する。
Since a small amount of filtered sand passes through the inner support wall 3 together with clear water, this sand is deposited as precipitated sand 91 in the settling cylinder 6.

第4図はろ送砂13と水を循環流によって動かす構成を
示しているが、ポンプ20の運転によって上室36の水
を吸入口82で吸入し吸引管26を通って一方は旋回タ
ンク9へ、一方はタンラメディ1最下部に設けた吐出口
90へ圧送する。
FIG. 4 shows a configuration in which the filter sand 13 and water are moved by a circulating flow. When the pump 20 is operated, the water in the upper chamber 36 is sucked in through the suction port 82, passes through the suction pipe 26, and one part goes to the swirling tank 9. , one side is fed under pressure to a discharge port 90 provided at the bottom of the tongue laminate 1.

圧送する水の量は各々弁21.24’に操作し、流量計
23.25で検知し、旋回タンク9内の汚濁水が逆流し
て上室36の汚染をしないように逆上弁22が設けられ
ている。
The amount of water to be pumped is controlled by each valve 21, 24' and detected by a flow meter 23, 25, and the backflow valve 22 is operated to prevent the contaminated water in the swirling tank 9 from flowing back and contaminating the upper chamber 36. It is provided.

上昇管8内には水が充満していて、エヤの管路49とエ
ヤ室50と細孔を経てエヤを上昇管8内に吐出すると、
気泡が上昇管8内を上昇し、この上昇流によって充満し
ている水に上昇流が発生する。
The riser pipe 8 is filled with water, and when air is discharged into the riser pipe 8 through the air conduit 49, air chamber 50, and pores,
The bubbles rise in the riser pipe 8, and this upward flow generates an upward flow in the water filled with the air.

一方、ろ過室31内のろ送砂13は下シュート7の空隙
85.86から少鼠宛落下しく矢印sg。
On the other hand, the filtration sand 13 in the filtration chamber 31 is falling from the gap 85, 86 of the lower chute 7 to a small mouse as indicated by the arrow sg.

Sfに示す)底51を転動して下方域に堆積砂92とな
る。
Sf) rolls on the bottom 51 and becomes deposited sand 92 in the lower area.

上昇管8内の流速によりて、堆積砂92は浮揚し矢印s
h力方向至シろ送砂が上昇する。
Due to the flow velocity in the riser pipe 8, the accumulated sand 92 is floated as shown by the arrow s.
In the direction of the h force, the filtration sand rises.

ろ過室13内で捕捉した原水中の懸濁物はろ送砂13の
下降に迷れて下降をし、その多くは堆積砂92の中の含
有されていて、上昇管8内を上昇する(矢印WS)のは
水とエヤとろ送砂と懸濁物でろる。
The suspended matter in the raw water captured in the filtration chamber 13 gets lost in the downward movement of the filtration sand 13 and descends, and most of it is contained in the deposited sand 92 and rises in the riser pipe 8 (as indicated by the arrow) WS) is filtered by water, air, filtered sand, and suspended matter.

堆積砂92の汚濁度、量によって、或いはろ送砂の圧密
を防止するため、下室35全域に噴流を発生させての浄
化をする場合に#−i吐出ロ90から水を吐出させる。
Depending on the degree of contamination and amount of the deposited sand 92, or in order to prevent consolidation of the filtered sand, water is discharged from the #-i discharge chamber 90 when purifying the entire lower chamber 35 by generating a jet flow.

この吐出水は非常に有効で、空隙85.86を確実に確
保す゛る効果もめるし、下7&−ドアの内面とか沈殿筒
6の外周に生長するスライムのけ着を除去する効果など
がある。
This discharged water is very effective and has the effect of reliably securing the gaps 85 and 86, and has the effect of removing slime deposits that grow on the inner surface of the lower door 7 and the outer periphery of the settling tube 6.

これは、原水の処理量がダウンしたときにポンプ20と
弁24を操作しても、定期的に操作しても効果がろう、
処理量を一定に保って清澄水を得るために有効手段であ
る。
This will be effective whether the pump 20 and valve 24 are operated when the amount of raw water to be processed is down, or whether they are operated periodically.
This is an effective means for obtaining clear water while keeping the amount of treatment constant.

沈殿筒6内の沈殿砂91は定期的またはろ送砂13の入
替などのときに弁18を操作して抜き去る。
The settling sand 91 in the settling cylinder 6 is removed by operating the valve 18 periodically or when replacing the filtered sand 13.

上昇した汚濁水(矢印ws)h上昇W8の吐出口57か
ら噴出し、気泡は大気に開放され、水と砂と懸濁物が傘
54とシーート55を介して旋回タンク9内に放出され
る。
Rising polluted water (arrow ws) h is ejected from the discharge port 57 of the rising W8, air bubbles are released to the atmosphere, and water, sand, and suspended matter are discharged into the swirling tank 9 via the umbrella 54 and the sheet 55. .

旋回タンク9の吐出口59からの吐出水によって、円筒
52とコーン53の内面に旋回流が発生する。内方に近
い程、微細粒またf′ia濁物が集まシ、集水筒56を
介して排出管60を経て系外へ排出する。外方に近い程
、粗粒の砂(St )が集まるのでコーン53と上昇管
8との間隙58から下方へ砂を落下(sb )させる。
A swirling flow is generated on the inner surfaces of the cylinder 52 and the cone 53 by the water discharged from the discharge port 59 of the swirling tank 9 . The closer to the inside, the more fine particles or f'ia pollutants gather and are discharged to the outside of the system via the water collecting cylinder 56 and the discharge pipe 60. Since coarse sand (St) gathers closer to the outside, the sand falls (sb) downward from the gap 58 between the cone 53 and the riser pipe 8.

落下したろ送砂は第6図の矢印Saで示すように上シー
−)10を転動して、集水筒5の上板110に落下する
か転動矢印Sd、Ssを経てろ送砂の水中下での安息角
を形成する。矢印Sd+S@を経る間に粗粒なろ送砂は
ど転勤をし続けて外支持壁2側に集まる。
The fallen filter sand rolls on the upper seam 10 as shown by the arrow Sa in FIG. Forms the angle of repose underwater. While passing through the arrow Sd+S@, the coarse filtered sand continues to be transferred and gathers on the outer support wall 2 side.

この粗粒はど外支持壁2側に集まる構成が砂ろ過プロセ
スとして最大効果が挙る。懸濁物を捕捉する一次スクリ
ーンを粗粒なろ送砂とすると、砂と砂との間隙に大きい
懸濁物が捕捉されて二次スクリーンは形成されるが、小
さい懸濁物にこの二次スクリーンヲ・母スするので三次
スクリーンが形成されない。依って、砂ろ過する流速が
速くなき同等の原水質であれば充填する砂の量を少くで
きるし、ろ過室をコン・ダクトにすることも可能になる
のである。
The configuration in which the coarse particles gather on the side of the outer support wall 2 provides the greatest effect as a sand filtration process. If coarse-grained filter sand is used as the primary screen to trap suspended matter, large suspended matter will be trapped in the gaps between the sand and a secondary screen will be formed. Because of this, no tertiary screen is formed. Therefore, if the flow velocity for sand filtration is not fast and the raw water quality is the same, the amount of sand to be filled can be reduced, and the filtration chamber can also be made into a conductor.

原水室30に流入し^原水は外支持壁2を通過するか、
第5図、第6図に示す矢印萄方向の余剰原水となシ、合
流管65を経て集中マス42内に開口しfc噴出口12
0から噴出するように分流する。
Does the raw water flowing into the raw water chamber 30 pass through the outer support wall 2?
Excess raw water in the direction of the arrows shown in FIGS.
Divides the flow so that it ejects from 0.

この分流は、原水を供給口14に供給する手段としてポ
ンプ或いは自然流下によるが、原水室30の空間96へ
の供給量、供給圧力全一定化するのに有効である。従っ
て、空間96への原水の設定量と設定圧の確保が容易に
できるのである。
This branch flow uses a pump or gravity as a means for supplying the raw water to the supply port 14, but is effective in keeping the supply amount and supply pressure to the space 96 of the raw water chamber 30 constant. Therefore, it is possible to easily secure the set amount and pressure of raw water to the space 96.

また、更にほろ過操作を継続してろ過室31内が詰まり
几り、他の多くのどれかの管路が詰っ九すすると空間9
6への供給をストップしないと、トラブルが発生するが
、この分流方法を用いると自動的に噴出口120から原
水が噴出するので安全な操作をすることができる。
Furthermore, if the filtration operation is continued and the inside of the filtration chamber 31 becomes clogged, and any of the other pipes become clogged, the space 9 becomes clogged.
If the supply to 6 is not stopped, trouble will occur, but if this diversion method is used, the raw water will automatically be spouted from the spout 120, allowing safe operation.

〔発明の効果〕〔Effect of the invention〕

本発明の砂ろ過装置はろ過するためのろ送砂粒径を理想
的に配列するし、ろ送砂を下端部、上昇管内及び旋回タ
ンク内の3個所で洗浄するので、ろ送砂に付着し7を懸
濁物とかろ送砂に混在している懸濁物を分離する効果が
犬である。
The sand filtration device of the present invention ideally arranges the grain size of the filter sand for filtration, and cleans the filter sand at three locations: the lower end, the inside of the rising pipe, and the swirling tank, so it adheres to the sand. The effect of separating 7 from suspended matter and suspended matter mixed in the filter sand is the dog.

懸濁物を含む濃縮され念力濁水とスカム全系外に除去す
る手段を設け、砂洗浄の水を上室から取り出して内部循
環させるので、水の有効利用が計られる効果がある。
A means is provided to remove concentrated telekinetically turbid water and scum including suspended matter from the entire system, and water for sand washing is taken out from the upper chamber and circulated internally, which has the effect of effectively utilizing water.

コンパクトで簡易なろ過装置を以て高度な清澄水全得る
ことができ、時間的にも経済的にもより良い効果を得几
のである。
Highly clear water can be obtained using a compact and simple filtration device, which is more efficient in terms of time and economy.

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

第1図は本発明の外観正面図、 第2図は第1図の矢視A−人を示す側面図、第3図は第
1図の矢視B−Bで示される平面図、第4図は本発明の
概略構成を示し、 第5図は第4図の上室部分金示す詳細図、第6図は第4
図の砂層上方を示す詳細図、第7図は外支持壁2の孔部
を示す詳細立体図、第8図は外支持壁2の孔部断面を示
す詳細図、第9図は内支持壁3部分の断面を示す詳細図
、第10図は旋回タンク9への吐出水を得る部分の詳細
図。 第11図はタンクボディ1の下室付近を示す図、第12
図は原水の供給口を示す図、 第13図は第12図と対向する部分を示す図、1:タン
クボディ、2:外支持壁、3:内支持壁、9:旋回タン
ク、11:7アネル、12:伸縮管、13:砂、14:
供給口、15:排出口、20:ボンデ、30:原水室、
31:ろ過室、32:集水室、33:沈殿室、34:排
出室、35:下室、36二上室、52:円筒、53:コ
ーン、54:傘、74:滞流室、96:空間。 n下見板    77 下端    82吸入073孔
     兇外面    83開ロア4滞流室   乃
内面    路管 75仰角線    (イ)空隙 76水千線    81  空故 第11  図 85空隙     93 内面 あ空隙     %円板 87底      95 胴板 88細孔     % 空間 帥 フランジ     97  下端 美吐出口    郭 円弧板 91  沈殿砂    99  対向する位置92堆積
砂    ]0:l上板 第7図 第8図 第12図 第13図
Fig. 1 is an external front view of the present invention, Fig. 2 is a side view showing a person in the direction of arrow A in Fig. 1, Fig. 3 is a plan view shown in Fig. The figures show the schematic structure of the present invention, FIG. 5 is a detailed view showing the upper chamber part of FIG. 4, and FIG.
Figure 7 is a detailed three-dimensional view showing the hole in the outer support wall 2, Figure 8 is a detailed view showing the cross section of the hole in the outer support wall 2, and Figure 9 is the inner support wall. A detailed view showing a cross section of three parts, and FIG. 10 is a detailed view of a part that obtains water discharged to the swirling tank 9. FIG. 11 is a diagram showing the vicinity of the lower chamber of the tank body 1, and FIG.
The figure shows the raw water supply port, Figure 13 shows the part opposite to Figure 12, 1: Tank body, 2: Outer support wall, 3: Inner support wall, 9: Swivel tank, 11:7 Anel, 12: Telescopic pipe, 13: Sand, 14:
Supply port, 15: Discharge port, 20: Bonde, 30: Raw water chamber,
31: Filtration chamber, 32: Water collection chamber, 33: Precipitation chamber, 34: Discharge chamber, 35: Lower chamber, 36 Upper chamber, 52: Cylinder, 53: Cone, 54: Umbrella, 74: Retention chamber, 96 :space. n clapboard 77 lower end 82 suction 073 hole outer surface of box 83 open lower 4 retention chamber inner surface pipe 75 elevation line (a) void 76 water line 81 void No. 11 Figure 85 void 93 inner surface void % disk 87 bottom 95 Body plate 88 pores % Space width Flange 97 Lower end beautiful discharge port Circular arc plate 91 Sedimentation sand 99 Opposing position 92 Sedimentation sand ] 0:l Upper plate Fig. 7 Fig. 8 Fig. 12 Fig. 13

Claims (1)

【特許請求の範囲】 1、垂立する筒状のタンクボディ内にこれと同心状に外
方から内方へ外支持壁と内支持壁と集水筒と隔筒と上昇
管を設け、タンクボディと外支持壁外周面とがなす空間
を原水室とし外支持壁と内支持壁とがなす空間をろ過室
として砂を充填し、内支持壁と集水筒外周面とでなす空
間を集水室とし、集水室と隔筒外周面とでなす空間を排
出室とし、隔筒と上昇管外周面とでなす空間と前記ろ過
室とは下方で連通し、タンクボディの上方には上室を設
けて水表面を形成し下方には下室を設けるものからなる
砂ろ過装置において、 前記上昇管はタンクボディ内上部に伸びておりこの上昇
管上端に下広がり錐体状の傘を取付け、前記傘および上
昇管上部を収納する上部が筒状で下部が下絞りの錐体状
である旋回タンクを設けたことを特徴とする砂ろ過装置
。 2、前記上室の水平面上にファネルを位置調整可能に取
付け、前記ファネル下方に伸縮管、さらに前記伸縮管下
方に吐出管を連結したことを特徴とする特許請求の範囲
第1項記載の砂ろ過装置。 3、下室は下拡がりの下シュートとタンクボディの底と
で形成し、前記下室内に集水室と連通する沈澱筒を設け
、この沈澱筒とタンクボディの底を貫通するドレン管に
弁を設けることを特徴とする特許請求の範囲第1項記載
の砂ろ過装置。
[Scope of Claims] 1. An outer support wall, an inner support wall, a water collection pipe, a partition pipe, and a rising pipe are provided concentrically from the outside to the inside in a vertically cylindrical tank body, and the tank body The space formed by the outer supporting wall and the outer circumferential surface of the outer supporting wall is used as a raw water chamber, the space formed between the outer supporting wall and the inner supporting wall is used as a filtration chamber, and is filled with sand, and the space formed by the inner supporting wall and the outer circumferential surface of the water collecting cylinder is used as a water collecting chamber. The space formed by the water collection chamber and the outer circumferential surface of the bulkhead is the discharge chamber, the space formed by the bulkhead and the outer circumferential surface of the riser pipe and the filtration chamber communicate with each other downwardly, and an upper chamber is provided above the tank body. In the sand filtration device, the riser pipe extends to the upper part of the tank body, and a cone-shaped umbrella that spreads downward is attached to the upper end of the riser pipe. A sand filtration device characterized by being provided with a rotating tank whose upper part is cylindrical and whose lower part is conical with a lower aperture for storing the umbrella and the upper part of the riser pipe. 2. The sand according to claim 1, characterized in that a funnel is mounted on the horizontal surface of the upper chamber so that its position can be adjusted, a telescopic pipe is connected below the funnel, and a discharge pipe is connected below the telescopic pipe. Filtration device. 3. The lower chamber is formed by a lower chute that expands downward and the bottom of the tank body, and a sedimentation tube that communicates with the water collection chamber is provided in the lower chamber, and a valve is installed in the drain pipe that passes through this sedimentation tube and the bottom of the tank body. A sand filtration device according to claim 1, characterized in that it is provided with:
JP60137342A 1985-06-24 1985-06-24 Sand filter Expired - Lifetime JPH06164B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60137342A JPH06164B2 (en) 1985-06-24 1985-06-24 Sand filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60137342A JPH06164B2 (en) 1985-06-24 1985-06-24 Sand filter

Publications (2)

Publication Number Publication Date
JPS621415A true JPS621415A (en) 1987-01-07
JPH06164B2 JPH06164B2 (en) 1994-01-05

Family

ID=15196401

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60137342A Expired - Lifetime JPH06164B2 (en) 1985-06-24 1985-06-24 Sand filter

Country Status (1)

Country Link
JP (1) JPH06164B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011016070A (en) * 2009-07-08 2011-01-27 Kurita Water Ind Ltd Adsorption column

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011016070A (en) * 2009-07-08 2011-01-27 Kurita Water Ind Ltd Adsorption column

Also Published As

Publication number Publication date
JPH06164B2 (en) 1994-01-05

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