JP3391498B2 - Gravity filtration device - Google Patents

Gravity filtration device

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Publication number
JP3391498B2
JP3391498B2 JP06090093A JP6090093A JP3391498B2 JP 3391498 B2 JP3391498 B2 JP 3391498B2 JP 06090093 A JP06090093 A JP 06090093A JP 6090093 A JP6090093 A JP 6090093A JP 3391498 B2 JP3391498 B2 JP 3391498B2
Authority
JP
Japan
Prior art keywords
filter medium
opening
pipe
water
backwash
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP06090093A
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Japanese (ja)
Other versions
JPH06246108A (en
Inventor
寛 本橋
真一郎 江川
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.)
Ebara Corp
Original Assignee
Ebara Corp
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Filing date
Publication date
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Priority to JP06090093A priority Critical patent/JP3391498B2/en
Publication of JPH06246108A publication Critical patent/JPH06246108A/en
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Publication of JP3391498B2 publication Critical patent/JP3391498B2/en
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Links

Description

【発明の詳細な説明】 【0001】 【産業上の利用分野】本発明は、上水、下水、工業用
水、その他の液体を濾過浄化するための重力式濾過装置
に関する。 【0002】 【従来の技術】通常、重力式濾過装置においては、濾過
中に捕捉した濁質の蓄積により濾過抵抗が増大した濾材
層を逆洗することが行われるが、その際に、まず濾材層
の下部から空気を圧入して濾材層を流動撹拌する空気洗
浄が行われている。 【0003】この濾材層の空気洗浄に先立ち、あらかじ
め槽内の水位を逆洗排水樋の上端よりも十分に下げてお
かないと、下部から圧入した空気によって水面が膨張
し、流動状態となった濾材が逆洗排水樋中に溢流し、濾
材の損失をきたす。そのために、濾過装置に機械的、電
気的制御装置を付属させ、槽内水位を下げるための特別
な操作を行っていた。 【0004】また、このような制御装置や操作をできる
だけ簡便にすべく、実公昭60−22964号公報に示
されるように、逆洗排水樋と濾材層との間の側壁に排水
弁を備えた中間排水管を開口させたものも提案されてい
る。 【0005】 【発明が解決しようとする課題】しかしながら、槽内水
位を逆洗排水樋よりも十分下げるため、例えばアンスラ
サイトや活性炭を濾材に使用した場合には、濾材層の表
面から約200mm以下の側壁に中間排水管を開口させる
と、槽内水の流出により水平流(横流れ)が発生する。
この水平流によって濾材層表面に位置する濾材が流動化
しはじめ、中間排水管から濾材が流出し、特に水平流に
よって濾材が移動するようになると、濾材層表面に位置
する濾材が相互摩擦によって多量に流出することにな
る。 【0006】このような濾材流出を防止するため、実開
昭61−155009号及び実開昭60−112312
号において、傾斜面を有する排水路(実開昭61−15
5009号)又は傾斜した液抜き管(実開昭60−11
2312号)を設置することが提案されている。しかし
ながら、上記公報に記載したものは、いずれも傾斜した
部分(斜面又は管)で濾材の流出を防止するとともに濾
材層に戻そうとする考えをとっているのみであり、排水
の流速については考慮されていなかったため、流速によ
って濾材が流出するという問題点があった。この傾向は
軽い濾材に特に顕著にみられる。 【0007】本発明は上述の事情に鑑みなされたもの
で、前記空気洗浄に先立ち、中間排水管により槽内水を
排水する際に、濾材を流出させることなく水位を十分に
低下させることができる重力式濾過装置を提供すること
を目的とする。 【0008】 【課題を解決するための手段】前述した目的を達成する
ため本発明は、槽内の逆洗排水樋と濾材層の間に中間排
水管を開口させた重力式濾過装置において、前記中間排
水管に中間排水管の開口よりも広い開口面積を有した開
口部を連設し、この開口部に複数の傾斜板又は傾斜管を
け、前記複数の傾斜板又は傾斜管の水平面よりの傾斜
角度を40°〜80°の範囲内に設定したことを特徴と
するものである。 【0009】 【作用】上記構成の本発明では、空気洗浄に先立ち、槽
内水位を逆洗排水樋より下げるべく中間排水管から槽内
水を槽外に排出する時に、中間排水管の開口に連設され
た開口部に傾斜板又は傾斜管が設置されているから、濾
材層の表層面近くの横流れ現象が極めて少なくなり、ま
た開口部から流入した排水中の濾材は傾斜板又は傾斜管
のみかけの平均流速の減速作用によって分離され傾斜面
に沿って落下し、濾材層に最終的に戻る。このように濾
材が分離された排水は中間排水管を通り系外へ流出し、
濾材の流出防止は効果的に行われる。また、傾斜板又は
傾斜管に加えて、中間排水管の開口より大きい開口面積
を有した開口部の排水の減速作用によって、濾材の流出
防止はさらに効果的になる。 【0010】このように、中間排水管の開口部を設定す
ることによって、アンスラサイトや活性炭の濾材層で
は、開口面を濾材層の表面から50mm程度の距離までに
下げても濾材流出防止効果がある。 【0011】 【実施例】以下、本発明に係る重力式濾過装置の一実施
例を図面を参照しながら説明する。図1は濾過装置の全
体構成を示す図であり、同図において、槽1内は垂直仕
切壁2によって濾過室3と排水渠4に仕切られ、濾過室
3の底部には濾過水を集水する集水室5が形成されてい
る。そして、集水室5の上部にはアンスラサイト、砂、
活性炭その他の濾材を充填した濾材層6が支持され、濾
材層6の上方に逆洗排水樋7が設けられ、その一端は排
水渠4に連通されている。 【0012】濾過室3の集水室5には、濾過水流出管兼
逆洗水管8が接続され、この濾過水流出管兼逆洗水管8
には濾過水流出弁9及び逆洗弁10が設けられ、さらに
集水室5には空気洗浄のための空気弁11を備えた空気
流入管12が接続されている。また、排水渠4には、逆
洗排水弁13を備えた逆洗排水管14が接続されてい
る。 【0013】また、垂直仕切壁2をまたいでサイフォン
管からなる中間排水管15が配置されており、この中間
配水管15の一端は濾過室3内の逆洗排水樋7と濾材層
6の間に開口され、他端は排水渠4内に開口、水封され
ている。そして、中間配水管15の開口15aには、図
2にその詳細が示されるように、開口15aより広い開
口面積を有した開口部16が連設されており、この開口
部16内に複数の平板状の傾斜板17が列設されてい
る。 【0014】前記傾斜板17の水平面よりの傾斜角度
(θ)は、40゜〜80°の範囲内に設定され、好まし
くは60°に設定されている。さらに、中間排水管15
の頂部にはサイフォン真空管18が連結され、このサイ
フォン真空管18はサイフォン真空弁19を介して真空
ポンプ20に連通されると共に、サイフォン真空管18
にはサイフォン破壊弁21が設けられている。なお、符
号22は水位電極を示す。 【0015】次に、前述のように構成された重力式濾過
装置の作用を説明する。濾過中、槽1内に導入された原
水は、重力により濾材層6を下向きに通過し、その間に
原水中の濁質が捕捉され、濾過水は集水室5から濾過水
流出管兼逆洗水管8を経て外部に流出する。かかる濾過
を継続するにしたがって、濾材層6は捕捉した濁質の蓄
積によって濾過抵抗が増し、所定の抵抗値に達した時点
で濾材層6の逆洗を行う。 【0016】逆洗に当たっては、原水の導入を停止し、
まず、槽内水位を逆洗排水樋7よりも十分下げるため、
サイホン作用により中間排水管15を介して逆洗排水管
14から槽内水を外部へ排出する。槽内水が中間排水管
15に連設された開口部16に流入すると、排水中に含
まれる濾材粒子Pは図3に示されるように傾斜板17に
向かって進行する。即ち、開口部16内の中間排水の流
速をVt、濾材粒子Pの沈降速度をVsとすると、濾材
粒子PはVtとVsを合成した進行速度Voで傾斜板1
7に向かって進行する。そして、濾材粒子Pは傾斜板1
7に衝接した後、傾斜板17に沿って沈降し濾材槽6に
最終的に戻る。即ち、開口部16に設置した傾斜板17
の作用によって、中間排水のみかけの平均流速が減速さ
れるため、濾材の槽外への流出が防止される。 【0017】これに加えて、開口部16は、中間排水管
15の開口15aより広い開口面積になっているため、
開口部16を流れる中間排水の流速は中間排水管15内
のそれよりも減速されている。そのため、前述した中間
排水の平均流速Vtは中間排水管15内の平均流速より
も小さくなり、この点からも濾材の槽外への流出が防止
される。このように、本発明によれば、傾斜板17によ
る中間排水のみかけの平均流出を減速することによる濾
材流出防止作用と、中間排水管15の開口15aよりも
広い開口面積を有した開口部16による平均流速を減速
することによる濾材流出防止作用の相乗効果が期待で
き、軽い濾材であっても流出が防止される。 【0018】上述のようにして中間排水管15からの排
水が終了した後、サイホンを破壊し空気流入管12から
集水室5内に空気を圧入し、濾材層6を流動撹拌させて
捕捉している濁質を剥離する。この間、槽内水位が十分
に下がっているために流動する濾材が逆洗排水樋7に溢
流することはない。 【0019】次いで、空気流入管12からの空気の圧入
を継続しながら逆洗弁10から濾過水流出管兼逆洗水管
8を経て集水室5に洗浄水を導入し、空気,水の同時洗
浄を行った後、次に空気流入管12からの空気の圧入を
停止させて水洗浄を行って、濾材層6を洗浄し、剥離さ
れた濁質と共に逆洗排水は逆洗排水樋7へ溢流し、排水
渠4を経て逆洗排水管14から外部へ排出される。この
ようにして、所定時間濾材層6の逆洗を行ったのち、濾
過操作を再開する。 【0020】図4は本発明の他の実施例を示し、中間排
水管15に連設された開口部を略円錘台状の開口部と
し、この開口部に同心状の傾斜板を設置したものであ
る。図4(a)は開口部の断面図、図4(b)は底面図
である。図4に示されるように、中間排水管15の開口
15aには略円錘台状の開口部26が連設され、この開
口部26に複数の傾斜板27が円心状に配置されてい
る。傾斜板27の傾斜角度(θ)は図2の傾斜板17と
同様に設定されている。なお、開口部26の中心部26
aはデッドゾーンである。本実施例の作用効果は図2に
示す第1実施例と同様である。 【0022】図5は本発明の更に他の実施例を示し、図
5(a)及び図5(b)は開口部を底面からみた図であ
り、開口部には傾斜板に代えて傾斜管が設置されてい
る。図5(a)に示す実施例においては、開口部36に
四角形断面を有する多数の傾斜管37が格子状に設置さ
れている。また、図5(b)に示す実施例においては、
開口部46に六角形断面を有する多数の傾斜管47がハ
ニカム状に設置されている。傾斜管37,47の傾斜角
度(θ)は図2の傾斜板17と同様に設定されている。 【0023】このように、開口部36又は46に傾斜管
37又は47を設置することによって、図2乃至図4に
示す傾斜板17,27と同様な作用効果が得られるとと
もに、排水の整流効果が期待できる。 【0024】 【発明の効果】以上述べたように本発明によれば、濾材
層の空気洗浄に先立ち、槽内水位を逆洗排水樋の上端よ
りも十分に下げることができ、しかも濾材の流出を効果
的に防止し、空気洗浄を支障なく行うことができるもの
である。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gravity filter for filtering and purifying clean water, sewage, industrial water, and other liquids. 2. Description of the Related Art Generally, in a gravity filtration apparatus, a filter medium layer having an increased filtration resistance due to accumulation of turbid matter trapped during filtration is backwashed. Air washing is performed in which air is injected from the lower part of the bed to flow and stir the filter medium bed. [0003] Prior to washing the filter medium layer with air, unless the water level in the tank is sufficiently lowered beforehand from the upper end of the backwash drainage gutter, the water surface expands due to the air injected from the lower part and becomes a fluid state. The filter media overflows into the backwash drain gutter, causing loss of the filter media. For that purpose, a mechanical and electrical control device was attached to the filtration device, and a special operation for lowering the water level in the tank was performed. Further, in order to make such a control device and operation as simple as possible, as shown in Japanese Utility Model Publication No. 60-22964, a drain valve is provided on a side wall between a backwash drainage gutter and a filter medium layer. One that opens an intermediate drain pipe has also been proposed. [0005] However, in order to lower the water level in the tank sufficiently below the backwash drain gutter, for example, when anthracite or activated carbon is used for the filter medium, it is about 200 mm or less from the surface of the filter medium layer. When an intermediate drain pipe is opened on the side wall of the tank, horizontal flow (lateral flow) occurs due to outflow of water in the tank.
Due to this horizontal flow, the filter medium located on the surface of the filter medium layer begins to fluidize, and the filter medium flows out of the intermediate drain pipe. Will be leaked. In order to prevent such outflow of the filter medium, Japanese Utility Model Laid-Open No. Sho 61-155509 and Japanese Utility Model Laid-Open No. Sho 60-112312 have been proposed.
No., a drainage channel with an inclined surface
No.5009) or inclined drain pipe (Jpn.
No. 2312). However, those described in the above-mentioned publications are merely designed to prevent the outflow of the filter medium at the inclined portion (slope or pipe) and to return the filter medium to the filter medium layer. Therefore, there is a problem that the filter medium flows out depending on the flow rate. This tendency is particularly noticeable in light filter media. The present invention has been made in view of the above-mentioned circumstances, and it is possible to sufficiently lower the water level without draining out a filter medium when draining water in a tank by an intermediate drain pipe prior to the air cleaning. It is an object to provide a gravity filtration device. [0008] In order to achieve the above-mentioned object, the present invention relates to a gravity type filtration device having an intermediate drainage pipe opened between a backwash drainage gutter in a tank and a filter medium layer. an opening having a wider opening area than the opening of the intermediate discharge pipe consecutively provided to the intermediate discharge pipe, only <br/> setting a plurality of inclined plates or inclined tube into the opening, the plurality of inclined plate or inclined Inclination of pipe from horizontal plane
The angle is set in the range of 40 ° to 80 ° . According to the present invention having the above-mentioned structure, prior to air cleaning, when water in the tank is discharged from the intermediate drain pipe to the outside of the tank in order to lower the water level in the tank from the backwash drain gutter, the opening of the intermediate drain pipe is opened. Since the inclined plate or inclined pipe is installed in the continuous opening, the lateral flow phenomenon near the surface layer of the filter medium layer is extremely reduced, and the filter medium in the drainage flowing from the opening is It is separated by the deceleration of the apparent average flow velocity, falls along the inclined surface, and finally returns to the filter medium layer. The wastewater from which the filter media has been separated in this way flows out of the system through the intermediate drainage pipe,
The prevention of the outflow of the filter medium is effectively performed. Further, in addition to the inclined plate or the inclined pipe, the drainage of the opening having an opening area larger than the opening of the intermediate drainage pipe can reduce the drainage of the filter medium more effectively. As described above, by setting the opening of the intermediate drain pipe, in the filter medium layer of anthracite or activated carbon, even if the opening surface is reduced to a distance of about 50 mm from the surface of the filter medium layer, the effect of preventing the filter medium from flowing out is obtained. is there. An embodiment of a gravity filter according to the present invention will be described below with reference to the drawings. FIG. 1 is a view showing the overall configuration of a filtration device. In FIG. 1, the inside of a tank 1 is partitioned by a vertical partition wall 2 into a filtration chamber 3 and a drainage channel 4, and filtered water is collected at the bottom of the filtration chamber 3. A collecting water chamber 5 is formed. And anthracite, sand,
A filter medium layer 6 filled with activated carbon or another filter medium is supported, and a backwash drainage gutter 7 is provided above the filter medium layer 6, and one end thereof is connected to the drainage ditch 4. A filtered water outflow pipe and a backwash water pipe 8 are connected to the water collecting chamber 5 of the filtration chamber 3.
Is provided with a filtered water outflow valve 9 and a backwash valve 10, and further connected to the water collecting chamber 5 is an air inflow pipe 12 provided with an air valve 11 for air cleaning. Further, a backwash drain pipe 14 having a backwash drain valve 13 is connected to the culvert 4. An intermediate drainage pipe 15 composed of a siphon pipe is disposed across the vertical partition wall 2. One end of the intermediate drainage pipe 15 is provided between the backwash drainage gutter 7 in the filtration chamber 3 and the filter medium layer 6. And the other end is opened and drained in the culvert 4. As shown in detail in FIG. 2, an opening 16 having an opening area larger than the opening 15 a is provided continuously with the opening 15 a of the intermediate water distribution pipe 15. Flat inclined plates 17 are arranged. The inclination angle (θ) of the inclined plate 17 from the horizontal plane is set in the range of 40 ° to 80 °, and is preferably set to 60 °. Further, the intermediate drain pipe 15
Is connected to a vacuum pump 20 via a siphon vacuum valve 19, and a siphon vacuum tube 18 is connected to the top of the siphon vacuum tube 18.
Is provided with a siphon break valve 21. Reference numeral 22 denotes a water level electrode. Next, the operation of the gravity-type filtration device configured as described above will be described. During filtration, the raw water introduced into the tank 1 passes downward through the filter medium layer 6 due to gravity, and during this time, turbidity in the raw water is captured. It flows out through the water pipe 8. As the filtration is continued, the filtration resistance of the filter medium layer 6 increases due to the accumulation of the trapped turbidity. When the resistance reaches a predetermined resistance value, the filter medium layer 6 is backwashed. In backwashing, the introduction of raw water is stopped,
First, in order to lower the water level in the tank sufficiently below the backwash drain gutter 7,
The water in the tank is discharged to the outside from the backwash drainage pipe 14 via the intermediate drainage pipe 15 by the siphon action. When the tank water flows into the opening 16 connected to the intermediate drain pipe 15, the filter medium particles P contained in the drain water advance toward the inclined plate 17 as shown in FIG. That is, assuming that the flow velocity of the intermediate wastewater in the opening 16 is Vt and the sedimentation velocity of the filter medium particles P is Vs, the filter medium particles P are inclined at a traveling speed Vo obtained by combining Vt and Vs.
Proceed towards 7. And the filter medium particles P are inclined plate 1
After abutment with the filter 7, it sinks down along the inclined plate 17 and finally returns to the filter medium tank 6. That is, the inclined plate 17 installed in the opening 16
By this, the apparent average flow velocity of the intermediate wastewater is reduced, so that the outflow of the filter medium out of the tank is prevented. In addition, since the opening 16 has an opening area larger than the opening 15a of the intermediate drain pipe 15,
The flow rate of the intermediate drainage flowing through the opening 16 is slower than that in the intermediate drainage pipe 15. Therefore, the above-mentioned average flow velocity Vt of the intermediate drainage is smaller than the average flow velocity in the intermediate drainage pipe 15, and from this point, the outflow of the filter medium out of the tank is also prevented. As described above, according to the present invention, the filter medium outflow preventing action by decelerating the apparent average outflow of the intermediate drainage by the inclined plate 17 and the opening 16 having an opening area larger than the opening 15 a of the intermediate drainage pipe 15. Therefore, a synergistic effect of the filter medium outflow preventing action by reducing the average flow velocity can be expected, and outflow can be prevented even with a light filter medium. After the drainage from the intermediate drain pipe 15 is completed as described above, the siphon is broken, air is injected into the water collecting chamber 5 from the air inlet pipe 12, and the filter medium layer 6 is flow-stirred and captured. Exfoliate suspended matter. During this time, the flowing filter medium does not overflow into the backwash drainage gutter 7 because the water level in the tank is sufficiently lowered. Next, while continuing press-in of the air from the air inlet pipe 12, washing water is introduced from the backwash valve 10 into the collecting chamber 5 through the filtered water outlet pipe and the backwash water pipe 8, and the air and water are simultaneously injected. After the cleaning, the press-in of the air from the air inflow pipe 12 is stopped to perform water cleaning to wash the filter medium layer 6, and the backwash drainage together with the separated turbidity is sent to the backwash drainage gutter 7. It overflows and is discharged to the outside from the backwash drainage pipe 14 through the drainage channel 4. After the filter medium layer 6 is backwashed for a predetermined time in this way, the filtration operation is restarted. FIG. 4 shows another embodiment of the present invention, in which the opening connected to the intermediate drain pipe 15 is a substantially frustoconical opening, and a concentric inclined plate is installed in this opening. Things. FIG. 4A is a sectional view of the opening, and FIG. 4B is a bottom view. As shown in FIG. 4, a substantially frustum-shaped opening 26 is continuously provided at the opening 15 a of the intermediate drain pipe 15, and a plurality of inclined plates 27 are arranged in a circular shape at the opening 26. . The inclination angle (θ) of the inclined plate 27 is set similarly to the inclined plate 17 of FIG. The center 26 of the opening 26
a is a dead zone. The operation and effect of this embodiment are the same as those of the first embodiment shown in FIG. FIG. 5 shows still another embodiment of the present invention, and FIGS. 5 (a) and 5 (b) are views of the opening viewed from the bottom. Is installed. In the embodiment shown in FIG. 5A, a large number of inclined tubes 37 having a square cross section are provided in the opening 36 in a lattice shape. In the embodiment shown in FIG.
A large number of inclined tubes 47 having a hexagonal cross section are installed in the opening 46 in a honeycomb shape. The inclination angles (θ) of the inclined tubes 37 and 47 are set in the same manner as the inclined plate 17 of FIG. By arranging the inclined pipes 37 or 47 in the openings 36 or 46 in this manner, the same operation and effects as those of the inclined plates 17 and 27 shown in FIGS. Can be expected. As described above, according to the present invention, the water level in the tank can be sufficiently lowered from the upper end of the backwash drainage gutter prior to the air cleaning of the filter medium layer, and the outflow of the filter medium can be achieved. Can be effectively prevented, and air cleaning can be performed without any trouble.

【図面の簡単な説明】 【図1】本発明に係る重力式濾過装置の一実施例を示す
断面図である。 【図2】本発明に係る重力式濾過装置における中間排水
管に連設された開口部を示す断面図である。 【図3】本発明に係る重力式濾過装置の作用を示す説明
図である。 【図4】本発明の重力式濾過装置の他の実施例を示す図
であり、図4(a)は断面図、図4(b)は底面図であ
る。 【図5】本発明の更に他の実施例を示す底面図であり、
図5(a)は格子状に傾斜管を配置した例、図5(b)
はハニカム状に傾斜管を配置した例である。 【符号の説明】 1 槽 2 垂直仕切壁 3 濾過室 4 排水渠 5 集水室 6 濾材層 7 逆洗排水樋 8 濾過水流出管兼逆洗水管 9 濾過水流出弁 10 逆洗弁 11 空気弁 12 空気流入管 13 逆洗排水弁 14 逆洗排水管 15 中間排水管 16,26,36,46 開口部 17,27 傾斜板 18 サイフォン真空管 19 サイフォン真空弁 20 真空ポンプ 37,47 傾斜管
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a sectional view showing one embodiment of a gravity filtration device according to the present invention. FIG. 2 is a sectional view showing an opening connected to an intermediate drain pipe in the gravity filtration device according to the present invention. FIG. 3 is an explanatory view showing the operation of the gravity filtration device according to the present invention. FIG. 4 is a view showing another embodiment of the gravity filtration device of the present invention, wherein FIG. 4 (a) is a sectional view and FIG. 4 (b) is a bottom view. FIG. 5 is a bottom view showing still another embodiment of the present invention;
FIG. 5A shows an example in which inclined tubes are arranged in a grid pattern, and FIG.
Is an example in which inclined tubes are arranged in a honeycomb shape. [Description of Signs] 1 tank 2 vertical partition wall 3 filtration room 4 drainage ditch 5 water collection room 6 filter medium layer 7 backwash drainage gutter 8 filtered water outflow pipe and backwash water pipe 9 filtered water outflow valve 10 backwash valve 11 air valve 12 Air inflow pipe 13 Backwash drain valve 14 Backwash drain pipe 15 Intermediate drain pipe 16, 26, 36, 46 Opening 17, 27 Inclined plate 18 Siphon vacuum pipe 19 Siphon vacuum valve 20 Vacuum pump 37, 47 Incline pipe

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B01D 24/46 B01D 24/02 B01D 29/62 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 7 , DB name) B01D 24/46 B01D 24/02 B01D 29/62

Claims (1)

(57)【特許請求の範囲】 【請求項1】 槽内の逆洗排水樋と濾材層の間に中間排
水管を開口させた重力式濾過装置において、前記中間排
水管に中間排水管の開口よりも広い開口面積を有した開
口部を連設し、この開口部に複数の傾斜板又は傾斜管を
け、前記複数の傾斜板又は傾斜管の水平面よりの傾斜
角度を40°〜80°の範囲内に設定したことを特徴と
する重力式濾過装置。
(57) [Claim 1] In a gravity filtration device having an intermediate drainage pipe opened between a backwash drainage gutter and a filter medium layer in a tank, an opening of the intermediate drainage pipe is provided in the intermediate drainage pipe. consecutively provided an opening having a wider opening area than, <br/> set only a plurality of inclined plates or inclined tube into the opening, the inclination of the horizontal plane of the plurality of inclined plate or inclined tube
A gravity filtration device, wherein the angle is set within a range of 40 ° to 80 ° .
JP06090093A 1993-02-25 1993-02-25 Gravity filtration device Expired - Fee Related JP3391498B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06090093A JP3391498B2 (en) 1993-02-25 1993-02-25 Gravity filtration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06090093A JP3391498B2 (en) 1993-02-25 1993-02-25 Gravity filtration device

Publications (2)

Publication Number Publication Date
JPH06246108A JPH06246108A (en) 1994-09-06
JP3391498B2 true JP3391498B2 (en) 2003-03-31

Family

ID=13155699

Family Applications (1)

Application Number Title Priority Date Filing Date
JP06090093A Expired - Fee Related JP3391498B2 (en) 1993-02-25 1993-02-25 Gravity filtration device

Country Status (1)

Country Link
JP (1) JP3391498B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101475805B1 (en) * 2013-05-15 2014-12-23 안준홍 Prevent sedimentation coolant tank
JP6535708B2 (en) * 2017-08-04 2019-06-26 株式会社神鋼環境ソリューション Water treatment device, runoff control method of filter medium
JP6989482B2 (en) * 2018-12-06 2022-01-05 株式会社東芝 Filtration device and filter media outflow control unit

Also Published As

Publication number Publication date
JPH06246108A (en) 1994-09-06

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