JPH02241508A - Filtration apparatus with both upward and downward flows - Google Patents

Filtration apparatus with both upward and downward flows

Info

Publication number
JPH02241508A
JPH02241508A JP6119889A JP6119889A JPH02241508A JP H02241508 A JPH02241508 A JP H02241508A JP 6119889 A JP6119889 A JP 6119889A JP 6119889 A JP6119889 A JP 6119889A JP H02241508 A JPH02241508 A JP H02241508A
Authority
JP
Japan
Prior art keywords
water
filtration
filter medium
pipe
raw water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP6119889A
Other languages
Japanese (ja)
Inventor
Koichi Hanai
花井 浩一
Yasuo Hamada
浜田 泰男
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.)
SHINKO PANTETSUKU KANKYO KANRI KK
Original Assignee
SHINKO PANTETSUKU KANKYO KANRI KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SHINKO PANTETSUKU KANKYO KANRI KK filed Critical SHINKO PANTETSUKU KANKYO KANRI KK
Priority to JP6119889A priority Critical patent/JPH02241508A/en
Publication of JPH02241508A publication Critical patent/JPH02241508A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To contrive an improvement in capacity and to make filter media washed easily and surely by packing a floating filter medium and a sinking filter medium into a filtration tank equipped with a supply port for an original water at its middle part so as to make a filtration possible both in upward and downward directions. CONSTITUTION:An original water is filled into a filtration chamber 1a through a supply port 8 and separates a floating filter medium 6 and a sinking filter medium 7 upward and downward from each other due to a density difference between them. Two filter medium layers are, therefore, formed both at the top and the bottom of the chamber 1a. The original water is divided into upward and downward flows, which are filtered by layers of the floating filter medium 6 and the sinking filter medium 7 respectively. When a rate of filtration becomes slow, a pump P is stopped, the original water is made to flow reversely and discharged through the supply port 8 and a discharge pipe 12 until a water level arrives at a lower limit L of a water level gauge 15. Next, a washing air is ejected into the original water by a blower B, the floating filter medium 6 and the sinking filter medium 7 are agitated for the sake of having suspended substances, which are attached to them, removed, and the original water containing those substances is discharged out the discharge pipe 12. The washing of filter media is finished and the filtration process is reopened, after the original water is once again supplied into the filtration chamber 1a, the aeration washing is repeated for a short time and the original water containing remaining suspended substances is discharged.

Description

【発明の詳細な説明】 〔産業上の利用分野] 本発明は、河川水や産業排水等の汚濁水中に含まれる懸
濁物質を除去するに用いられる上下双方向流濾過装置に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to an up-and-down bidirectional flow filtration device used to remove suspended matter contained in polluted water such as river water or industrial wastewater.

〔従来の技術〕[Conventional technology]

従来、河川水や産業排水等の汚濁水中に含まれる懸濁物
質を除去する濾過袋2は、通常、粒状の濾材を用い、か
つ濾過により汚れた粒状濾材を装置内で逆洗して再浄化
し得る構成とされてある。
Conventionally, the filter bag 2 that removes suspended solids contained in polluted water such as river water or industrial wastewater usually uses granular filter media, and the granular filter media contaminated by filtration is backwashed within the device to repurify it. It is possible to do so.

そして、これら従来の濾過装置には、その濾過の方向に
よって類別すると、原水の送給口の下方に濾材を単層ま
たは複層に配し、原水を下方に向けて濾過する最も一般
的な■下向流濾過装置。
These conventional filtration devices are categorized according to the direction of filtration. Downflow filtration device.

原水の送給口の上方に水より比重の小さい粒状濾材(以
降、浮上濾材という)を単層に配し〔特開昭60−10
6511.61−187908号〕、または、浮上濾材
と水より比重の大きい粒状濾材(以降、沈下濾材という
)とを復層に配し〔特開昭59− 123505. 6
2−38214号〕、原水を上方に向けて濾過する■上
向流濾過装置.原水の送給口を上下双方に設けると共に
、中間部に配した濾材層の層内から取水して、上下双方
から中間に向けて濾過する■上下対向流濾過装置〔実公
昭58−33764号、特開昭48−50352.59
−95907号〕等がある。
A single layer of granular filter media (hereinafter referred to as floating filter media) with a specific gravity smaller than that of water is arranged above the raw water supply port [JP-A-60-10
6511.61-187908], or a floating filter medium and a granular filter medium (hereinafter referred to as a sinking filter medium) having a higher specific gravity than water are arranged in a reverse layer [JP-A-59-123505. 6
2-38214], ■ Upward flow filtration device that filters raw water upward. ■Vertical counterflow filtration device [Utility Model Publication No. 58-33764, Japanese Patent Publication No. 48-50352.59
-95907] etc.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

濾過装置の処理能力は、その濾過面積に比例するので、
上記従来の■下向流濾過装置や■上向流濾過装置のよう
に、単一方向に濾過する方式では、上記従来の■上下対
向流濾過装置に比べて半分の1Ita能力しか得られな
い。
The processing capacity of a filtration device is proportional to its filtration area, so
In a system that filters in a single direction, such as the above-mentioned conventional (1) downward flow filtration device and (2) upward flow filtration device, only half the capacity of 1 Ita can be obtained compared to the above-mentioned conventional (2) vertical counterflow filtration device.

一方、中間部に配した濾材層の層内から取水する上記従
来の■上下対向流濾過装置においては、その濾過面積を
■下向流濾過装置や■上向流濾過装置に比して倍増させ
得るものの、粒状の濾材を用いる場合、その逆洗時に、
濾材が個々の重さおよび粒径にて分級されて上下に差を
もって配列され、逆洗後に再構成される濾材層が上下で
濾過損失に差が生じるため、上下均等な原水の配分が行
えなくなり、濾過面積の倍増に見合う濾過能力の向上が
得られないという問題がある。
On the other hand, in the above-mentioned conventional vertical counterflow filtration device that takes water from within the filter media layer placed in the middle, the filtration area is doubled compared to the downward flow filtration device and the upflow filtration device. However, when using granular filter media, when backwashing it,
The filter media is classified by individual weight and particle size and arranged with a difference in the top and bottom, and the filter media layer that is reconstituted after backwashing causes a difference in filtration loss between the top and bottom, making it impossible to distribute raw water evenly in the top and bottom. However, there is a problem in that the filtration capacity cannot be improved commensurately with doubling the filtration area.

また、上部に浮上濾材を、下部に沈下濾材を配する一方
、これらの中間部に原水を投入して、上下双方向に濾過
する方式が考えられるが、この場合には、濾過槽の上部
と下部の双方に集水機構を設けることが必要となるため
、逆洗水を下方または上方から濾過槽内に送給して濾材
を洗浄したとしても、濾材洗浄により懸濁物質濃度の高
まった逆洗水を、上方または下方から排出させると、上
部または下部の集水機構が汚染されて、爾後の濾過に支
障が生じるという事態を招き、また、この逆洗水を、中
間部から排出させようとした場合、濾材が逆洗水に随伴
して流失することを防ぐために濾材ストレーナが必要と
なり、反面、濾材ストレーナを濾過層内に設けると、こ
の濾材ストレーナが懸濁物質に汚染されて閉塞したり、
逆洗水に随伴して流出せんとする濾材により閉塞したり
するため、頻繁な清掃を行わない限り逆洗水の円滑な排
出が行えない等の弊害があり、濾材の洗浄に関連する維
持管理が困難となることより、装置としては実用化され
るまでに至っていなかった。
Another possible method is to place a floating filter medium in the upper part and a sinking filter medium in the lower part, and then input raw water into the middle part of the tank to filter it in both directions, but in this case, the upper part of the filtration tank and Since it is necessary to provide a water collection mechanism on both sides of the lower part, even if backwash water is sent into the filtration tank from below or above to clean the filter media, the backwash water, which has an increased concentration of suspended solids due to filter media cleaning, will If the wash water is discharged from the top or bottom, the water collection mechanism at the top or bottom will be contaminated and subsequent filtration will be hindered. In this case, a filter media strainer is required to prevent the filter media from being washed away along with backwash water. On the other hand, if a filter media strainer is provided in the filtration layer, the filter media strainer may become contaminated with suspended matter and become clogged. Or,
Because the filter media that tries to flow out with the backwash water becomes clogged, there are problems such as the backwash water not being able to be drained smoothly unless frequent cleaning is performed, and maintenance and management related to filter media cleaning. However, due to the difficulties involved, it has not been put into practical use as a device.

本発明は上記従来の濾過装置における問題点を解消し得
る、すなわち、上下双方向に濾過し得て処理能力の向上
が図れ、しかも、濾材の洗浄も容易かつ確実に行い得る
上下双方向流濾過装置の提供を目的とするものである。
The present invention can solve the above-mentioned problems with the conventional filtration device, that is, it can filter both up and down, improving processing capacity, and the filter medium can be easily and reliably washed. The purpose is to provide equipment.

〔課題を解決するための手段〕[Means to solve the problem]

上記目的を達成するために、本発明は以下の構成として
いる。すなわち、その第1発明の上下双方向流濾過装置
は、上部および下部に集水機構を設け、中間部に原水の
送給口を設けた濾過槽内に、水より比重の小さい粒状濾
材と、水より比重の大きい粒状濾材とを充填し、かつ、
上部の集水機構に連通ずる上濾過木管に吸・排気管を接
続分岐させ、下部の集水機構に連通ずる下濾過水管に洗
浄用空気供給管を接続分岐させる一方、原水の送給口に
連通ずる給水管に排水管を接続分岐させると共に、原水
の送給口と排水管との間の給・排水共用管路部に粒状濾
材の流失防止用ストレーナを設けたものである。
In order to achieve the above object, the present invention has the following configuration. That is, the vertical two-way flow filtration device of the first invention includes a granular filter medium having a specific gravity smaller than that of water, and a filtration tank having a water collection mechanism in the upper and lower parts and a raw water supply port in the middle part. filled with a granular filter medium having a specific gravity greater than that of water, and
The suction and exhaust pipes are connected and branched to the upper filtration pipe connected to the upper water collection mechanism, and the cleaning air supply pipe is connected and branched to the lower filtration water pipe connected to the lower water collection mechanism, while the raw water supply port is connected and branched. A drain pipe is connected and branched to a communicating water supply pipe, and a strainer for preventing granular filter media from being washed away is provided in the common water supply/drainage pipe between the raw water supply port and the drain pipe.

また、第2発明の上下双方向流濾過装置は、上記の構成
に加え、下部の集水機構に連通ずる下濾過水管に、逆洗
用水供給管を接続分岐させたものである。
In addition to the above-described configuration, the second invention provides a two-way flow filtration device in which a backwash water supply pipe is connected and branched to the lower filtration water pipe communicating with the lower water collection mechanism.

〔作用〕[Effect]

本発明の上下双方向流濾過装置においては、濾過槽内に
、水より比重の小さい粒状濾材と、水より比重の大きい
粒状濾材とを充填しているので、濾過槽の中間部に設け
た給水口から内部に原水を送給することにより、濾過槽
内上部に水より比重の小さい粒状濾材からなる濾材層を
、下部に水より比重の大きい粒状濾材からなる濾材層を
形成させて、上下双方向に濾過し得る。また、上下双方
向に濾過することで、上または下向流濾過装置のように
単一方向に濾過する方式に比べ、同容量の濾過槽にて二
倍の濾過面積を得ることができる。
In the up-and-down bidirectional flow filtration device of the present invention, the filtration tank is filled with granular filter media whose specific gravity is smaller than that of water and granular filter media whose specific gravity is larger than that of water. By feeding raw water into the interior through the mouth, a filter layer made of granular filter media with a specific gravity smaller than that of water is formed in the upper part of the filtration tank, and a filter media layer made of granular filter media with a higher specific gravity than water is formed in the lower part of the filtration tank. It can be filtered in the opposite direction. Furthermore, by filtrating in both directions, it is possible to obtain twice the filtration area in a filtration tank of the same capacity as in a single direction filtration system such as an upward or downward flow filtration device.

また、上部と下部に集水機構を設けているのでこれら上
部および下部集水機構それぞれに連通ずる上および下濾
過水管を経る濾過水の流量を調整することで、上下双方
向の濾過量を容易に均等化し得る。
In addition, since the upper and lower water collection mechanisms are provided, the flow rate of filtrate through the upper and lower filtration water pipes that communicate with the upper and lower water collection mechanisms can be adjusted to easily increase the amount of filtration in both directions. can be equalized to

以下、本発明の上下双方向流濾過装置における粒状濾材
の洗浄について、その工程に沿い説明する。まず、原水
の送給を停止し、原水の送給口に連通ずる給水管に接続
分岐させた排水管から、濾過槽内の原水を所定量排水す
る一方、上部集水機構に連通ずる上濾過水管に接続分岐
させた吸・排気管から、濾過槽内上部に空気を吸入させ
る。そして、濾過槽内水位を上部の集水機構の下端より
低くする。
Hereinafter, cleaning of the granular filter medium in the up-and-down bidirectional flow filtration device of the present invention will be explained along the steps. First, the supply of raw water is stopped, and a predetermined amount of raw water in the filtration tank is drained from a branched drain pipe that is connected to a water supply pipe that communicates with the raw water supply port. Air is sucked into the upper part of the filtration tank through the intake and exhaust pipes that are connected to the water pipes and branched. Then, the water level in the filtration tank is set lower than the lower end of the upper water collection mechanism.

次いで、下部集水機構に連通ずる下濾過水管に接続分岐
させた洗浄用空気供給管から、濾過槽内に洗浄用空気を
送給する一方、上部集水機構に連通ずる上濾過水管に接
続分岐させた吸・排気管から排気させる。この洗浄用空
気の送給・排出にて濾過槽内に形成される上向き空気流
により、濾過槽内の粒状濾材は攪拌されて、互いに衝突
・摩擦し合うので、これら粒状濾材の表面に捕捉されて
いた懸濁物質は、剥離させられて濾過槽内の原水中に懸
濁する。この洗浄用空気の送給に際して、上部集水機構
は水面上にあり、懸濁物質濃度の増した濾過槽内の原水
に接触して汚染されることがな(、一方、下部集水機構
は、洗浄用空気により逆洗される。
Next, cleaning air is supplied into the filtration tank from the cleaning air supply pipe that is connected to and branched off from the lower filtration water pipe that communicates with the lower water collection mechanism, while the air supply pipe is connected and branched to the upper filtration water pipe that communicates with the upper water collection mechanism. Exhaust air from the intake and exhaust pipes. The upward air flow that is formed in the filtration tank by the supply and discharge of this cleaning air agitates the granular filter media in the filtration tank, causing them to collide and rub against each other. The suspended solids are separated and suspended in the raw water in the filtration tank. When supplying this cleaning air, the upper water collection mechanism is located above the water surface and is not contaminated by contact with the raw water in the filtration tank, which has an increased concentration of suspended solids (on the other hand, the lower water collection mechanism , backwashed by cleaning air.

次いで、給水口側から若干量の原水を濾過槽側に送給し
、原水の送給口と排水管との間の給・配水共用管路部に
設けられた粒状濾材の流失防止用ストレーナを逆洗する
。これは、上記の洗浄用空気の送給・排出により攪拌さ
れた粒状濾材が、流失防止用ストレーナに侵入して、次
に述べる原水の排水に際して目見まりの原因となること
を予防するためであり、この逆洗で、流失防止用ストレ
ーナおよび該ストレーナと送給口との間の管路部に侵入
した粒状濾材は、濾過槽内に返送される。
Next, a small amount of raw water is sent from the water supply port side to the filtration tank side, and a strainer for preventing granular filter media from being washed away is installed in the common water supply/distribution pipe between the raw water supply port and the drain pipe. Backwash. This is to prevent the granular filter media stirred by the above-mentioned supply and discharge of cleaning air from entering the strainer to prevent runoff and causing clogging when draining raw water as described below. During this backwashing, the granular filter medium that has entered the strainer for preventing spillage and the pipe section between the strainer and the feed port is returned to the filtration tank.

次に、原水の送給口に連通ずる給水管に接続分岐させた
排水管から濾過槽内の原水を排水する。
Next, the raw water in the filtration tank is drained from a drain pipe that is connected to and branched from a water supply pipe that communicates with the raw water supply port.

この排水により、粒状ill過材から剥離された懸濁物
質は系外に排出・除去される。また、この排水に際して
、ili過槽内の粒状濾材は、原水の送給口と排水管と
の間の給・配水共用管路部に設けられた流失防止用スト
レーナに遮られて外部への流失を防止される。
By this drainage, the suspended solids separated from the granular ill filter material are discharged and removed from the system. In addition, during this drainage, the granular filter media in the ILI filtration tank is blocked by a strainer installed in the common water supply/distribution pipe between the raw water supply port and the drain pipe, preventing it from flowing out to the outside. will be prevented.

そして、上記に続き、給水管側から所定量の原水を濾過
槽内に再送給して、上記同様の空気洗浄、ストレーナ逆
洗、排水の洗浄工程を、数次に繰り返すことで、粒状濾
材から剥離された懸濁物質を確実に系外に排出・除去さ
せることができる。
Continuing from the above, a predetermined amount of raw water is re-feeded into the filtration tank from the water supply pipe side, and the same air cleaning, strainer backwashing, and drainage cleaning steps as described above are repeated several times to remove the granular filter media. The separated suspended solids can be reliably discharged and removed from the system.

また、第2発明の上下双方向流濾過装置においては、上
記の給水管側からの原水の再送給に代わり、下部集水機
構に連通ずる下濾過水管に接続分岐させた逆洗用水供給
管から逆洗水を送給し、濾過槽内を経て排水管から排水
することで、粒状濾過材から剥離された懸濁物質を系外
に効率良く排出・除去させることができる。
In addition, in the upper and lower two-way flow filtration device of the second invention, instead of re-feeding the raw water from the water supply pipe side as described above, from the backwash water supply pipe that is connected and branched to the lower filtration water pipe that communicates with the lower water collection mechanism. By supplying backwash water and discharging it from the drain pipe after passing through the filtration tank, suspended solids separated from the granular filter material can be efficiently discharged and removed from the system.

〔実施例〕〔Example〕

以下に、本発明の実施例を図面を参照して説明する。 Embodiments of the present invention will be described below with reference to the drawings.

第1図は本実施例の上下双方向流濾過装置の概念説明図
である。
FIG. 1 is a conceptual explanatory diagram of the up-and-down bidirectional flow filtration device of this embodiment.

第1図において、(1)は濾過槽であって、この濾過槽
(1)は、竪型の密閉容器とされ、その内部は、下部に
設けた隔壁(1b)にて、濾過室(1a)と、その下方
の集水室(1c)とに区画されである。
In FIG. 1, (1) is a filtration tank, and this filtration tank (1) is a vertical airtight container. ) and a water collection chamber (1c) below it.

この濾過槽(1)内の最上部には上部集水ストレーナ(
2)が設けてあり、一方、下部の隔壁(lb)には、複
数の下部集水ストレーナ(3)が配設され、濾過室(l
a)と集水室(1c)とは、これら下部集水ストレーナ
(3)を介して通水可能に連通されである。
At the top of this filtration tank (1) is an upper water collection strainer (
2), and on the other hand, a plurality of lower water collecting strainers (3) are arranged on the lower partition wall (lb), and a filtration chamber (lb) is provided.
a) and the water collection chamber (1c) are communicated with each other through these lower water collection strainers (3) so that water can flow therethrough.

また、これら下部集水ストレーナ(3)の直下方の隔壁
(lb)の下面には、円筒状の空気分配短管(3a)が
それぞれ縦設されてあり、また、各空気分配短管(3a
)の上下方向の中間部側壁には、第1図の部分拡大断面
図である第2図に示すように、オリフィス穴(3b)が
穿設されである。
In addition, cylindrical air distribution short pipes (3a) are installed vertically on the lower surface of the partition wall (lb) directly below these lower water collection strainers (3), and each air distribution short pipe (3a
As shown in FIG. 2, which is a partially enlarged cross-sectional view of FIG.

(4)は上濾過水管、(5)は下濾過水管であって、こ
れら上・下濾過水管(4)(5)は、上部集水ストレー
ナ(2)および集水室(lc)に連通され、かつ、それ
ぞれの中途に濾過水弁(4a) (5a)を設けると共
に、出側端を濾過水本管りに接続・合流させである。
(4) is an upper filtration water pipe, and (5) is a lower filtration water pipe, and these upper and lower filtration water pipes (4) and (5) are communicated with the upper water collection strainer (2) and the water collection chamber (LC). In addition, filtered water valves (4a) and (5a) are provided in the middle of each, and the outlet ends are connected to and merged with the filtered water main pipe.

(6)は浮上濾材であって、この浮上濾材(6)は、水
に浮く粒状物(具体的には、通常の上向流濾過方式に用
いられる発泡ポリスチレン粒、ボリプロピレン粒等)で
、図に示すように、濾過槽(1)内に送給された原水W
中にて浮上し、濾過槽(1)の濾過室(1a)上部で濾
材層を形成するものとされである。
(6) is a floating filter medium, and this floating filter medium (6) is a particulate material that floats on water (specifically, expanded polystyrene particles, polypropylene particles, etc. used in a normal upward flow filtration system), As shown in the figure, raw water W fed into the filtration tank (1)
It floats inside and forms a filter medium layer above the filtration chamber (1a) of the filtration tank (1).

(7)は沈下濾材であって、この沈下濾材(7)は、水
沈む粒状物(具体的には、通常の下向流濾過方式に用い
られる砂粒、アンスラサイト粒等)で、図に示すように
、濾過槽(1)内に送給された原水W中にて沈下し、濾
過槽(1)の濾過室(la)下部で濾材層を形成するも
のとされである。
(7) is a sinking filter medium, and this sinking filter medium (7) is a granular material that sinks in water (specifically, sand grains, anthracite grains, etc. used in normal downward flow filtration systems), as shown in the figure. As such, it sinks in the raw water W fed into the filtration tank (1) and forms a filter medium layer in the lower part of the filtration chamber (la) of the filtration tank (1).

(8)は原水送給口であって、この原水送給口(8)は
、濾過室(1a)下部の沈下濾材(7)が形成する濾材
層の上界面から少し上に位置する濾過槽(1)側壁を貫
通して設けられである。
(8) is a raw water supply port, and this raw water supply port (8) is connected to a filtration tank located slightly above the upper interface of the filter medium layer formed by the sinking filter medium (7) at the bottom of the filtration chamber (1a). (1) It is provided through the side wall.

(9)は濾材ストレーナであって、この濾材ストレーナ
(9)は、原水送給口(8)と原水ポンプPとを連通ず
る給水管G[Ilに取り付けられである。また、この濾
材ストレーナ(9)は原水送給口(8)に近接させて着
脱可能に設けられてあり、一方、給水管0ωには原水弁
(loa)が備えである。
(9) is a filter medium strainer, and this filter medium strainer (9) is attached to the water supply pipe G[Il that communicates the raw water supply port (8) and the raw water pump P. Further, this filter medium strainer (9) is removably installed in the vicinity of the raw water supply port (8), and on the other hand, the water supply pipe 0ω is equipped with a raw water valve (LOA).

00はバイパス管であって、このバイパス管00は、濾
材ストレーナ(9)の取り付は部の前後を結んで設けら
れてあり、濾材ストレーナ(9)が清掃等のため取り外
されたとき、原水Wの送給路としての役割を代行させる
ものである。なお、濾材ストレーナ(9)の前後および
バイパス管(11)の中間部には弁が設けられてあり、
これら弁の開閉操作により、濾過中においても濾材スト
レーナ(9)を取外して清掃できるものとされである。
00 is a bypass pipe, and this bypass pipe 00 has a filter medium strainer (9) installed by connecting the front and back of the part, and when the filter medium strainer (9) is removed for cleaning etc., the raw water is removed. This serves as a W feed path. In addition, valves are provided before and after the filter medium strainer (9) and in the middle part of the bypass pipe (11).
By opening and closing these valves, the filter medium strainer (9) can be removed and cleaned even during filtration.

02+は排水管゛であって、この排水管021は、排水
弁(12a)を備え、濾材ストレーナ(9)と原水弁(
10a)との間の給水管0[Dに接続分岐されである。
02+ is a drain pipe, and this drain pipe 021 is equipped with a drain valve (12a), and has a filter medium strainer (9) and a raw water valve (
10a) is connected to and branched from the water supply pipe 0[D].

03)は吸・排気管であって、この吸・排気管側は、フ
ロート弁(13a)を備え、濾過槽(+)直上方に位置
する上濾過水管(4)に接続分岐されである。
03) is an intake/exhaust pipe, and the intake/exhaust pipe side is equipped with a float valve (13a) and is connected to and branched from an upper filtration water pipe (4) located directly above the filtration tank (+).

(財)は空気供給管であって、この空気供給管側は、空
気弁(14a)を備え、濾過槽(1)の直下方の下濾過
水管(5)に接続分岐される一方、洗浄用空気の圧送用
ブロアBに連通されである。
(Incorporated) is an air supply pipe, and the air supply pipe side is equipped with an air valve (14a), and is connected and branched to the lower filtration water pipe (5) directly below the filtration tank (1), and is used for cleaning. It is connected to a blower B for pressure-feeding air.

Q5)は水位検出器であって、この水位検出器0ωは、
濾過層(1)向上部に配設され、上部集水ストレーナ(
2)下端より少し下に位置する玉検出水位L1と、この
玉検出水位Llの下方に位置する下検出水位L2とを検
出するものとされてあり、ここでは図示を省略した運転
制御装置に接続されである。
Q5) is a water level detector, and this water level detector 0ω is
The upper water collection strainer (
2) A ball detection water level L1 located slightly below the lower end and a lower detection water level L2 located below this ball detection water level Ll are detected, and are connected to an operation control device not shown here. It is.

00および面は流量計であって、これら流量計0007
)は、上濾過水管(4)および下濾過水管(5)の濾過
水弁(4a) (5a)より上流側に取り付けられであ
る。
00 and plane are flowmeters, and these flowmeters 0007
) is attached to the upper filtration water pipe (4) and the lower filtration water pipe (5) upstream of the filtration water valves (4a) and (5a).

側は逆洗水管であって、この逆洗水管面は、その一端を
、原水弁(10a)と原水ポンプP間の給水管θ0)に
接続され、他の一端を、濾過槽(1)と洗浄用空気供給
管(14間の下濾過水管(5)に接続され、その中間に
逆洗水弁(18a)を備えたものである。
The side is a backwash water pipe, and one end of this backwash water pipe surface is connected to the water supply pipe θ0) between the raw water valve (10a) and the raw water pump P, and the other end is connected to the filtration tank (1). It is connected to the lower filtration water pipe (5) between the cleaning air supply pipes (14), and is equipped with a backwash water valve (18a) in the middle.

09)および■は捨水管であって、これら捨水管OgJ
121は、上濾過水管(4)および下濾過水管(5)の
濾過水弁(4a) (5a)より上流側に接続分岐して
設けられ、それぞれ捨水弁(19a) (20a)を備
えたものである。
09) and ■ are drainage pipes, and these drainage pipes OgJ
121 is connected and branched on the upstream side of the filtrate valves (4a) and (5a) of the upper filtration water pipe (4) and the lower filtration water pipe (5), and is provided with a waste water valve (19a) and (20a), respectively. It is something.

なお、上記の各管路に備えた弁は、ここでは図示を省略
した運転制御装置により、その開閉を制御されるものと
されである。また、これら弁は、その開度を自由に設定
し得る構造で、その開度調整により流量を制御し得るも
のとされである。
Note that the opening and closing of the valves provided in each of the above-mentioned pipelines is controlled by an operation control device, which is not shown here. Further, these valves have a structure in which the degree of opening can be freely set, and the flow rate can be controlled by adjusting the degree of opening.

上記構成を具備する本実施例の上下双方向流濾過装置に
よる濾過および濾材洗浄について、それぞれの工程に沿
って、以下に詳述する。
Filtration and filter medium cleaning by the vertical two-way flow filtration device of this embodiment having the above configuration will be described in detail below along with each step.

(a)jlU!1 運転制御装置により、給水管0ωの原水弁(10a)と
上・下濾過水管(4) (5)の濾過水弁(4a) (
5a)を開に、排水管02)の排水弁(12a)と洗浄
用空気供給管070の空気弁(14a)を閉に作動させ
ると共に、原水ポンプPを運転して原水Wの圧送を開始
する。
(a) jlU! 1 The operation control device controls the raw water valve (10a) of the water supply pipe 0ω and the filtrate water valve (4a) of the upper and lower filtration water pipes (4) (5) (
5a) is opened, the drain valve (12a) of the drain pipe 02) and the air valve (14a) of the cleaning air supply pipe 070 are operated to close, and the raw water pump P is operated to start pumping the raw water W. .

原水ポンプPからの原水Wは、給水管0■および濾材ス
トレーナ(9)を介して濾過槽(1)側に送られ、原水
送給口(8)を経て濾過室(1a)内に充満すると共に
、この濾過室(la)P’7に充填されている浮上濾材
(6)と沈下濾材(7)とを比重差で上下に分離させて
、濾過室(1a)内の上下双方に濾材層を形成させる。
Raw water W from the raw water pump P is sent to the filtration tank (1) side via the water supply pipe 0■ and the filter medium strainer (9), and fills the filtration chamber (1a) through the raw water supply port (8). At the same time, the floating filter material (6) and the sinking filter material (7) filled in this filter chamber (la) P'7 are separated into upper and lower parts due to the difference in specific gravity, so that a filter material layer is formed on both the upper and lower sides of the filter chamber (1a). to form.

また、濾過室(la)内に送給された原水Wは、この濾
過室(1a)内で上下に分流させられる。そして、上向
きの原水Wは浮上濾材(6)Nを経て濾過されると共に
、上部集水ストレーナ(2)と上濾過水管(4)を経て
濾過水本管りに至り、一方、下向きの原水Wは沈下濾材
(7)層を経て濾過されると共に、下部集水ストレーナ
(3)を経て集水室(lc)に集合した後、下濾過水管
(5)を経て取水本管りに至り、この取水本管りで合流
して系外に排出される。
Moreover, the raw water W fed into the filtration chamber (la) is divided into upper and lower parts within this filtration chamber (1a). Then, the upward raw water W is filtered through the floating filter medium (6)N, and reaches the filtrate main pipe via the upper water collection strainer (2) and the upper filtration water pipe (4), while the downward raw water W The water is filtered through the sinking filter medium (7) layer, and after passing through the lower water collection strainer (3) and collecting in the water collection chamber (LC), it passes through the lower filtration water pipe (5) and reaches the water intake main pipe. They join together at the water intake main and are discharged outside the system.

このように、本実施例の上下双方向流濾過装置によれば
、原水Wを上下の双方向に濾過し得て、上または下向流
濾過装置のように単一方向に濾過する方式に比べ、同容
量の濾過槽にて二倍の濾過面積を得ることができて、そ
の濾過能力を倍増させることが可能となる。
As described above, the two-way up and down flow filtration device of this embodiment can filter the raw water W in both directions, up and down, compared to a system that filters in a single direction like an up or down flow filtration device. , it is possible to obtain twice the filtration area with a filtration tank of the same capacity, making it possible to double the filtration capacity.

なお、本実施例においては、上濾過水管(4)および下
濾過水管(5)を経て排出される濾過水量を、これら上
・下濾過水管(4)(5)に設けた流量計0007)に
て把握すると共に、それぞれの濾過水弁(4a) (5
a)の開度を調整することで、継続的に、上向き濾過水
量と下向き濾過水量とを均等化させた。
In this example, the amount of filtrate water discharged through the upper filtration water pipe (4) and the lower filtration water pipe (5) is measured by the flowmeter 0007) provided in these upper and lower filtration water pipes (4) and (5). At the same time, check each filtrate valve (4a) (5
By adjusting the opening degree of a), the amount of upward filtration water and the amount of downward filtration water were continuously equalized.

(b)櫨林援企 本実施例の上下双方向流濾過装置おいては、濾過の継続
により、その濾過速度がある程度まで低下したとき、以
下の工程により濾材洗浄を行う。
(b) Kashibayashi Enkaku In the up-and-down bidirectional flow filtration device of this embodiment, when the filtration speed decreases to a certain degree due to continued filtration, the filter medium is cleaned by the following steps.

■水抜工工程;原水ポンプPの運転を止めて、原水Wの
圧送を停止すると同時に、給水管0■の原水弁(10a
)と上・下濾過水管(4)(5)の濾過水弁(4a)(
5a)とを閉に作動させ、次に、排水管(+2)の排水
弁(12a)を開に作動させる。このとき、濾過室(1
a)内の沈下濾材(7)Nより上の原水Wは、原水送給
口(8)と濾材ストレーナ(9)を経て逆流して、排水
管(+2)から流出し始め、一方、濾過室(la)内の
水位低下により、吸・排気管面のフロート弁(13a)
のフロートが自動的に下降し、該フロート弁(13a)
が開の状態となり、吸・排気管0■を介して濾過室(1
a)内に空気が吸引される。続いて、濾過室(1a)内
の水位が、水位検出2W 05)の下検出水位L2まで
低下したとき、この水位検出器θωに接続された運転制
御装置を介して、排水管021の排水弁(12a)を閏
に作動させて、水抜き工程を終了する。
■Water drainage process; At the same time, stop the operation of the raw water pump P and stop pumping the raw water W, and at the same time, the raw water valve (10a) of the water supply pipe 0
) and the filtrate water valves (4a) (
5a) to close, and then open the drain valve (12a) of the drain pipe (+2). At this time, the filtration chamber (1
The raw water W above the sinking filter medium (7) N in a) flows backward through the raw water supply port (8) and the filter medium strainer (9) and begins to flow out from the drain pipe (+2), while the filtration chamber ( The float valve (13a) on the intake/exhaust pipe surface due to the drop in the water level in
The float automatically lowers and the float valve (13a)
is in the open state, and the filtration chamber (1
a) Air is drawn into. Subsequently, when the water level in the filtration chamber (1a) drops to the lower detection water level L2 of water level detection 2W 05), the drain valve of the drain pipe 021 is activated via the operation control device connected to this water level detector θω. (12a) is activated to complete the water removal process.

この水抜き工程の終了時点において、上部集水ストレー
ナ(2)は、濾過槽(1)の濾過室(1a)向上部に形
成される空気溜中に露出される。
At the end of this draining process, the upper water collection strainer (2) is exposed to the air pocket formed in the upper part of the filtration chamber (1a) of the filtration tank (1).

■空抜工丘;水抜き工程に続いて、空気供給管(財)の
空気弁(14a)を開に作動させる一方、ブロアBを運
転しての洗浄用空気の圧送を開始する。
■Draining process: Following the water draining process, the air valve (14a) of the air supply pipe is opened and the blower B is operated to start pumping the cleaning air.

ブロアBからの洗浄用空気は、空気供給管04と下濾過
木管(5)を経て濾過槽+1)の集水室(1c)内に送
られ、この集水室(lc)から、空気分配短管(3a)
で均等分配されつつ、下部集水ストレーナ(3)を経て
濾過室(la)内の原水W中に噴出させられる。
The cleaning air from blower B is sent into the water collection chamber (1c) of the filtration tank +1) via the air supply pipe 04 and the lower filtration wood pipe (5), and from this water collection room (lc), the air distribution short Pipe (3a)
The water is evenly distributed and ejected into the raw water W in the filtration chamber (la) through the lower water collection strainer (3).

そして、濾過室(1a)内の原水W中に噴出させれられ
た空気は、原水Wおよび原水W中の浮上濾材(6)と沈
下濾材(7)を激しく攪拌した後に、上部集水ストレー
ナ(2)、上濾過水管(4)、フロート弁(13a)お
よび吸・排気管Q3)を経て外部に排気される。
The air blown into the raw water W in the filtration chamber (1a) violently stirs the raw water W and the floating filter media (6) and sinking filter media (7) in the raw water W, and then flows through the upper water collection strainer ( 2), is exhausted to the outside via the upper filtration water pipe (4), the float valve (13a), and the intake/exhaust pipe Q3).

この空洗工程により、濾過室(la)の浮上濾材(6)
および沈下濾材(7)の表面に捕捉されていた懸濁物質
は、攪拌による浮上・沈下濾材(6) (7)同士の衝
突・摩擦により剥離させられて、濾過槽内の原水W中に
混合・懸濁させられる。また、この空洗工程において、
上部集水ストレーナ(2)は、原水Wの水面および浮上
濾材層(6)上面より高く位置しているので、攪拌用空
気の排出を阻害することがなく、かつ、懸濁物質濃度が
増加した原水Wと接触して汚される懸念がない。
Through this air washing step, the floating filter medium (6) in the filtration chamber (la)
The suspended solids trapped on the surface of the sinking filter media (7) are peeled off by the collision and friction between the floating filter media (6) and the sinking filter media (7) due to stirring, and are mixed into the raw water W in the filter tank.・Can be suspended. In addition, in this air washing process,
Since the upper water collection strainer (2) is located higher than the water surface of the raw water W and the upper surface of the floating filter layer (6), it does not impede the discharge of stirring air, and the suspended solids concentration increases. There is no fear of contamination due to contact with raw water W.

■′  ス レー ゛  q;空洗工程で攪拌された浮
上・沈下濾材(6)(7)は、濾材ストレーナ(9)お
よび該濾材ストレーナ(9)と原水送給口(8)との間
の給水管θω内に侵入し、これらが次工程の排水工程に
際して、源水W中の懸濁物質を捕1足して目詰まりの原
因となり、正常な排水が行えなくなる場合がある。本工
程は、このような事態が起こることを予防するために、
濾材ストレーナ(9)および給水管0(D内に侵入した
浮上・沈下濾材(6) (7)を、濾過室(1a)内に
返送する目的で行う。
■' Stray ゛q; The floating/sinking filter media (6) and (7) stirred in the air washing process are transferred to the filter media strainer (9) and between the filter media strainer (9) and the raw water supply port (8). They may enter the water supply pipe θω, and during the next drainage process, they may catch suspended solids in the source water W and cause clogging, making normal drainage impossible. In this process, in order to prevent such a situation from occurring,
This is done in order to return the floating/sinking filter media (6) (7) that have entered the filter media strainer (9) and water supply pipe 0 (D) into the filtration chamber (1a).

十分な空洗を行った後に、まず、ブロアBを停止させる
と共に、空気供給管04)の空気弁(14a)を閉に作
動させる0次いで、原水ポンプPを運転すると同時に、
原水弁(10a)を開に作動させ、原水Wを給水管aω
および濾材ストレーナ(9)を通じて濾過室(1a)内
に圧送する。
After sufficient air washing, first, the blower B is stopped and the air valve (14a) of the air supply pipe 04) is closed.Next, the raw water pump P is operated at the same time.
Open the raw water valve (10a) to supply raw water W to the water supply pipe aω.
and is pumped into the filtration chamber (1a) through the filter medium strainer (9).

これにより、濾材ストレーナ(9)および給水管0[D
内に侵入した浮上・沈下濾材(6) (7)は、原水W
に随伴して、濾過室(1a)内に返送される。
As a result, the filter medium strainer (9) and the water supply pipe 0 [D
The floating/sinking filter media (6) (7) that has entered the raw water W
is returned to the filtration chamber (1a).

そして、濾過室(la)内の水位が、水位検出器cつの
玉検出水位Llまで上昇したとき、この水位検出器0ω
に接続された運転制御装置により、原水ポンプPを停止
させると同時に、原水弁(10a)を閉に作動させる。
When the water level in the filtration chamber (la) rises to the water level Ll detected by the water level detector c, this water level detector 0ω
An operation control device connected to stops the raw water pump P and at the same time closes the raw water valve (10a).

このとき、濾過室(1a)内の水面は、上部集水ストレ
ーナ(2)の下端より少し下位置する水位検出2SOω
の玉検出水位L1の高さで止まるので、上部集水ストレ
ーナ(2)は懸濁物質濃度が増加した原水Wと接触して
汚される懸念がない。
At this time, the water level in the filtration chamber (1a) is located slightly below the lower end of the upper water collection strainer (2).
Since it stops at the height of the ball detection water level L1, there is no concern that the upper water collection strainer (2) will come into contact with the raw water W with an increased concentration of suspended solids and be contaminated.

■上水二程;濾材ストレーナ逆洗工程に続き、排水弁(
12a)を開に作動させて、濾過室(la)内の懸濁物
質濃度が増加した原水Wを、排水弁(12a)から排出
させる。このとき、濾過室(la)内の原水Wの水面は
徐々に低下して行き、この原水W中にて浮上する浮上濾
材(6)層の下端が原水送給、口(8)に達し、浮上濾
材(6)が原水送給口(8)を経て系外に流出しようと
するが、これらは濾材ストレーナ(9)に捕捉されて流
失することを防止される。
■Two steps of clean water; following the filter media strainer backwashing process, the drain valve (
12a) is operated to open, and the raw water W in which the concentration of suspended solids in the filtration chamber (la) has increased is discharged from the drain valve (12a). At this time, the water level of the raw water W in the filtration chamber (la) gradually decreases, and the lower end of the floating filter material (6) layer floating in this raw water W reaches the raw water supply port (8). Although the floating filter media (6) tries to flow out of the system through the raw water supply port (8), they are captured by the filter media strainer (9) and are prevented from flowing away.

■氷床工且;排水工程を終えた段階では、濾過室(+)
内の浮上濾材(6)の表面および沈下濾材(7)の間隙
には、懸濁物質が空洗時の濃度で残留しているので、以
下の水洗工程にて、残留懸濁物質を除去・排出して、浮
上・沈下濾材(6)を再浄化させる。
■Ice bed construction and; At the stage where the drainage process is finished, the filtration chamber (+)
Suspended substances remain on the surface of the floating filter medium (6) and in the gaps between the submerged filter medium (7) at the same concentration as during air washing, so the remaining suspended substances are removed and removed in the following water washing process. Discharge and repurify the floating/sinking filter medium (6).

まず、排水管0りの排水弁(loa)を閉に、給水管0
0)の原水弁(10a)を開に作動させると共に、原水
ポンプP@運転して、新たな原水Wを濾過室(1a)内
に再送給する。そして、濾過室(1a)内の水位が、水
位検出器θつの下検出水位L1に達したとき、原水ポン
プPの運転を停止させ、原水弁(10a)を閉に作動さ
せさせて、原水Wの再供給を止める。
First, close the drain valve (LOA) of the drain pipe, and
0) is opened, and the raw water pump P is operated to re-feed new raw water W into the filtration chamber (1a). When the water level in the filtration chamber (1a) reaches the lower detection water level L1 of the water level detector θ, the operation of the raw water pump P is stopped, the raw water valve (10a) is operated to close, and the raw water W stop resupplying.

次いで、前述の■空洗工程を短時間行い、浮上・沈下濾
材(6)(7)の表面および間隙に残留する懸濁物質を
、再供給した原水W中に混合・!Q濁させた後、前記の
■濾材ストレーナ逆洗工程を行い、続いて、前記の■排
水工程を行う。
Next, the above-mentioned (1) air washing process is performed for a short time, and the suspended solids remaining on the surfaces and gaps of the floating/sinking filter media (6) and (7) are mixed into the resupplied raw water W. Q After making it cloudy, perform the filter medium strainer backwashing step (1) described above, followed by the draining step (2) described above.

通常は、以上に述べた原水Wの再供給〜排水で、前記の
(a)濾過に復帰できるが、この■水洗工程のみで浮上
・沈下濾材(6)の洗浄が不十分な場合は、この■水洗
工程を数次に繰り返すことで、より十分な洗浄・再浄化
を達成することができる。
Normally, it is possible to return to the above-mentioned (a) filtration by resupplying and draining the raw water W as described above, but if the floating/sinking filter medium (6) is not sufficiently cleaned by this water washing step alone, ■By repeating the water washing process several times, more thorough cleaning and repurification can be achieved.

なお、濾材ストレーナ(9)は、送給および排出される
原水W中の懸濁物質により汚染されるが、送給される原
水Wによる汚れは排水される原水Wが逆洗の役割を果た
し、また、排水される原水Wによるlηれは送給される
原水Wが逆境の役割を果たすため、この濾材ストレーナ
(9)は、原水W中の懸濁物質により閉塞されることが
なく、常に正常に原水Wを流通させることができる。
Note that the filter medium strainer (9) is contaminated by suspended solids in the raw water W that is fed and discharged, but the raw water W that is drained plays the role of backwashing the dirt caused by the raw water W that is being fed. In addition, since the supplied raw water W plays an adverse role in lη leakage caused by the raw water W being drained, this filter medium strainer (9) is not blocked by suspended matter in the raw water W and is always in normal condition. The raw water W can be distributed to.

以上により、濾材洗浄を終了し、濾過を再開することが
できるが、より短時間に洗浄するには、上記の■水洗工
程に代わり、以下の■°逆逆上工程行う。
As described above, the filter medium cleaning can be completed and filtration can be resumed. However, in order to wash the filter medium in a shorter time, the following ② reverse upturn process is performed instead of the above ② water washing step.

前記の■排水工程の終了状態から、すなわち、吸・排気
管0■のフロート弁(13a)と、排水管021の排水
弁(12a)以外の各弁が閉じられた状態から、逆洗水
管08)の逆洗弁(18a)を開に作動させ、原水ポン
プPを運転して原水Wの送給を開始する。
From the state in which the above-mentioned drainage process (1) has been completed, that is, from the state in which all valves other than the float valve (13a) of the intake/exhaust pipe 0 (2) and the drain valve (12a) of the drain pipe 021 are closed, the backwash water pipe 08 ) is opened and the raw water pump P is operated to start supplying raw water W.

原水ポンプPからの原水Wは、逆洗水管0υと下部集水
管(5)を経て、濾過槽(1)の集水室(lc)内に送
られ、この集水室(lc)から、下部集水ストレーナ(
3)を経て、濾過室(la)内に噴出させられる。
Raw water W from the raw water pump P is sent to the water collection chamber (lc) of the filtration tank (1) via the backwash water pipe 0υ and the lower water collection pipe (5), and from this water collection chamber (lc), the water is sent to the lower water collection chamber (lc). Water collection strainer (
3) and is ejected into the filtration chamber (la).

そして、この原水Wは、下部集水ストレーナ(3)を逆
洗する一方、濾過室(1a)内の浮上・沈下濾材(6)
 (7)を攪拌しながら、これらの表面に残留している
懸濁物質を混合・懸濁させて取り込み、濾材ストレーナ
(9)を経て排水管(11)から流出する。
Then, this raw water W backwashes the lower water collection strainer (3), and the floating/sinking filter medium (6) in the filtration chamber (1a).
While stirring (7), the suspended substances remaining on the surfaces of these substances are mixed and suspended and taken in, and are discharged from the drain pipe (11) through the filter medium strainer (9).

この■°逆り工程により、濾過室(1a)内の浮上・沈
下濾材(6)(7)の表面および間隙に残留していた懸
濁物質は確実かつ効率良く系外に排出される。
By this reverse process, the suspended solids remaining on the surfaces and gaps of the floating/sinking filter media (6) and (7) in the filtration chamber (1a) are reliably and efficiently discharged from the system.

以上に述べた工程により、通常の濾材洗浄は終了し、濾
過が再開されるが、より清澄な濾過水が求められ、原水
による集水室(1c)および下部集水管(5)の汚染の
浄化が必要とされる場合には、濾過再開直後において、
上・下濾過水管(4) (5)の濾過水弁(4a) (
5a)を閉じると共に、捨水管0!D@の捨水弁(19
a) (20a)を開いて、捨水管09)elから濾過
水を捨水し、この捨水が清澄になった後に、濾過水本管
り側に濾過水を流して、正常な濾過に移行する。
Through the steps described above, normal filter medium cleaning is completed and filtration is restarted, but clearer filtered water is required, and the contamination of the water collection chamber (1c) and lower water collection pipe (5) by raw water is purified. If necessary, immediately after restarting filtration,
Upper and lower filtration water pipes (4) (5) filtrate water valve (4a) (
5a) and close the drainage pipe 0! D@'s drainage valve (19
a) Open (20a) and drain the filtered water from the drain pipe 09)el, and after the drained water becomes clear, flow the filtered water to the filtrate main pipe side to proceed to normal filtration. do.

二のように、本実施例の上下双方向流濾過装置によれば
、濾過により濾材に捕捉された!A濁動物質、効率良く
洗浄して系外に排出・除去し得て、容易に濾過効率の復
元が図れ、しかも、洗浄水の水源および送給ポンプを一
元化し得て、その構成を簡易なものとし得る。
As shown in No. 2, according to the up-and-down bidirectional flow filtration device of this embodiment, it was captured by the filter medium during filtration! A: Turbid substances can be efficiently washed and discharged/removed from the system, filtration efficiency can be easily restored, and the water source and feed pump for washing water can be unified, making the configuration simple. It can be taken as a thing.

なお、本実施例の上下双方向流濾過装置においては、よ
り清澄な濾過水が求められる場合に行われる通常の濾過
水による逆洗も可能である。
In addition, in the vertical bidirectional flow filtration device of this embodiment, backwashing with normal filtered water, which is performed when clearer filtered water is required, is also possible.

すなわち、前述の■排水工程または■水洗工程に続き、
集水本管り側から濾過水を逆送させて、濾過室(1a)
内に送給する一方、これを排水管0りから排出させるこ
とで、通常の濾過水による逆洗を行うことができる。こ
の場合、集水本管り側から逆送される濾過水は、濾過水
弁(4a)および(5a)の開閉により、上部集水管(
4)と下部集水管(5)とに任意に分配し得るので、浮
上濾材(6)1!および沈下濾材(7)双方の逆洗を同
時に行うこともできる。
In other words, following the above-mentioned ■drainage process or ■water washing process,
The filtered water is sent back from the main water collection side to the filtration chamber (1a).
By discharging this water from the drain pipe, normal backwashing with filtered water can be performed. In this case, the filtered water that is sent back from the main water collection pipe is controlled by the opening and closing of the filtrate valves (4a) and (5a).
4) and the lower water collection pipe (5), the floating filter medium (6) 1! It is also possible to backwash both the submerged filter medium (7) and the submerged filter medium (7) at the same time.

また、本実施例の上下双方向流濾過装置においては、逆
洗水管0IIDを原水ポンプに連通させ、原水Wにて逆
洗するものとしたが、これは、別に設けられた水源およ
び供給手段に連通され、他の逆洗水にて逆洗するもとさ
れても良い。
In addition, in the up-and-down bidirectional flow filtration device of this embodiment, the backwash water pipe 0IID is connected to the raw water pump, and backwashing is performed with raw water W. It may also be connected and used as a source for backwashing with other backwash water.

〔発明の効果〕〔Effect of the invention〕

以上に述べたように、本発明の上下双方向流濾過装置に
よれば、原水を上下の双方向に濾過し得て、上または下
向流i1.!過装置のような単一方向に濾過する方式に
比べ、同−容量の濾過槽にて二倍の濾過面積を得ること
ができて、その濾過能力を倍増させることが可能となり
、しかも、濾過により濾材に捕捉された懸濁物質を、確
実かつ効率良く洗浄して系外に排出・除去し得て、容易
に濾過効率の復元が図れるので、濾材の洗浄に係わる維
持管理が簡単となり、更には、洗浄水の水源および送給
ポンプを一元化し得て、その構成を簡易なものとし得る
等々の顕著な効果が達成できる。
As described above, according to the up-and-down bidirectional flow filtration device of the present invention, raw water can be filtered in both the up and down directions, and the upward or downward flow i1. ! Compared to a method that filters in a single direction such as a filtration device, it is possible to obtain twice the filtration area with a filtration tank of the same capacity, making it possible to double the filtration capacity. The suspended solids trapped in the filter media can be reliably and efficiently washed, discharged and removed from the system, and the filtration efficiency can be easily restored, which simplifies maintenance and management related to cleaning the filter media. It is possible to achieve remarkable effects such as being able to unify the water source of the washing water and the feed pump, and simplifying the configuration.

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

第1図は本発明の実施例の上下双方向流濾過装置の概念
説明図、 第2図は第1図の部分拡大断面図、 (1)−濾過槽、 (1bL−隔壁、 (2)−上部集水スト (3)−下部集水スト (4)−上濾過木管、 (6)−浮上濾材、 (8)−原水送給口、 00)−給水管、 側−吸・排気管、 051−水位検出器、 B−ブロア、 P−原水ポンプ、 (la)−一濾過室、 (lc)−−集水室、 レーづ・、 レーナ、 (5)−下濾過水管、 (7)−沈下濾材、 (9)−濾材ストレーナ、 021−排水管、 θ4−空気供給管、 08)−逆洗水管、 D−濾過水本管、 W−原水。 特許出願人 神鋼ファウドラー環境管理株式会社代 理
 人 弁理士  金丸 章− 手υε(重圧(l(自発) 1.事件の表示 平成1年特許願第611913号 2、発明の名称 上下双方向流譚過装置 3、補正をする者 事j牛との関係     特許出願人 件 所   神戸市中央区脇浜町1丁ロ4′fi78号
名 称   神鋼ファウドラー環境管理株式会社代表者
  片 山 栄 − 郵便番号 657 神戸市灘区岩屋北町5丁目1番3号 日清青写真ビル4F 4、代理人 住所 6、補正の対象 明細書の「発明の詳細な説明」の欄 7、補正の内容 (1)  明細書第17頁第17行目に「濾過槽内の」
とあるところを「濾過室(1a)内の」と補正する。 (2)  明細書第20頁第5行目に「浮上・沈下濾材
(6)を」とあるところを「浮上・沈下°濾材(6)(
7)を」と補正する。 (3)  明細書第20頁第6行目に「排水弁(10a
)を閉に、」とあるところを「排水弁(12a)を閉に
、」と補正する。 (4)  明細書第20頁第10行目に「下検出水位L
1に」とあるところを「下検出水位L2に」と補正する
。 (5)  明!Ill書第20頁第20行目に「浮上・
沈下濾材(6)の」とあるところを「浮上・沈下濾材(
6)(7)のjと補正する。 (6)  明細書第22頁第8行目「排水管(II)か
ら」とあるところを「排水管0りから21と補正する。 以上
FIG. 1 is a conceptual explanatory diagram of a vertical two-way flow filtration device according to an embodiment of the present invention, and FIG. 2 is a partially enlarged sectional view of FIG. 1. Upper water collection station (3) - Lower water collection station (4) - Upper filtration wood pipe, (6) - Floating filter medium, (8) - Raw water supply port, 00) - Water supply pipe, Side - Suction/exhaust pipe, 051 -Water level detector, B-Blower, P-Raw water pump, (LA)--Filtration chamber, (LC)--Water collection chamber, Lena, (5)-Lower filtration water pipe, (7)-Sinking Filter medium, (9) - Filter medium strainer, 021 - Drain pipe, θ4 - Air supply pipe, 08) - Backwash water pipe, D - Filtered water main pipe, W - Raw water. Patent Applicant: Shinko Faudler Environmental Management Co., Ltd. Agent: Akira Kanamaru, Patent Attorney: Hand υε (heavy pressure (l)) 1. Display of the incident 1999 Patent Application No. 611913 2, Name of the invention Device 3, Person making the correction Relationship with the cow Patent applicant Location 1-4'fi78, Wakihama-cho, Chuo-ku, Kobe Name Name: Shinko Faudler Environmental Management Co., Ltd. Representative Sakae Katayama - Postal code: 657 Nada, Kobe City Nissin Blueprint Building 4F 4, 5-1-3 Iwaya Kitamachi, Ward 4, Agent Address 6, “Detailed Description of the Invention” column 7 of the specification to be amended, Contents of the amendment (1) Page 17 of the specification In line 17, “in the filtration tank”
The text has been corrected to read "inside the filtration chamber (1a)." (2) On page 20, line 5 of the specification, the phrase “floating/sinking filter medium (6)” was replaced with “floating/sinking filter medium (6) (
7)”. (3) On page 20, line 6 of the specification, “Drain valve (10a
) should be closed," should be corrected to read, "The drain valve (12a) should be closed." (4) “Lower detection water level L” on page 20, line 10 of the specification
1" is corrected to "lower detection water level L2." (5) Ming! Book Ill, page 20, line 20 says, “Levitation.
Where it says “Sinking filter media (6)”, replace it with “Floating/Sinking filter media (
6) Correct j in (7). (6) On page 22 of the specification, line 8, the phrase “from drain pipe (II)” is amended to read “from drain pipe 0 to 21.”

Claims (2)

【特許請求の範囲】[Claims] (1)上部および下部に集水機構を設け、中間部に原水
の送給口を設けた濾過槽内に、水より比重の小さい粒状
濾材と、水より比重の大きい粒状濾材とを充填し、かつ
、上部の集水機構に連通する上濾過水管に吸・排気管を
接続分岐させ、下部の集水機構に連通する下濾過水管に
洗浄用空気供給管を接続分岐させる一方、原水の送給口
に連通する給水管に排水管を接続分岐させると共に、原
水の送給口と排水管との間の給・排水共用管路部に粒状
濾材の流失防止用ストレーナを設けたことを特徴とする
上下双方向流濾過装置。
(1) Filling a filtration tank with a water collection mechanism in the upper and lower parts and a raw water supply port in the middle part with a granular filter medium having a specific gravity lower than that of water and a granular filter medium having a specific gravity higher than that of water, In addition, the suction and exhaust pipes are connected and branched to the upper filtration water pipe that communicates with the upper water collection mechanism, and the cleaning air supply pipe is connected and branched to the lower filtration water pipe that communicates with the lower water collection mechanism, while raw water is supplied. A drain pipe is connected and branched to the water supply pipe communicating with the mouth, and a strainer for preventing granular filter media from being washed away is provided in the common supply/drainage pipe between the raw water supply port and the drain pipe. Up and down bidirectional flow filtration device.
(2)下部の集水機構に連通する下濾過水管に、逆洗用
水供給管を接続分岐させたことを特徴とする第1請求項
記載の上下双方向流濾過装置。
(2) The vertical bidirectional flow filtration device according to claim 1, characterized in that a backwash water supply pipe is connected and branched to the lower filtration water pipe communicating with the lower water collection mechanism.
JP6119889A 1989-03-13 1989-03-13 Filtration apparatus with both upward and downward flows Pending JPH02241508A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6119889A JPH02241508A (en) 1989-03-13 1989-03-13 Filtration apparatus with both upward and downward flows

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6119889A JPH02241508A (en) 1989-03-13 1989-03-13 Filtration apparatus with both upward and downward flows

Publications (1)

Publication Number Publication Date
JPH02241508A true JPH02241508A (en) 1990-09-26

Family

ID=13164240

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6119889A Pending JPH02241508A (en) 1989-03-13 1989-03-13 Filtration apparatus with both upward and downward flows

Country Status (1)

Country Link
JP (1) JPH02241508A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014240050A (en) * 2013-06-12 2014-12-25 扶桑建設工業株式会社 Biological contact filtration apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014240050A (en) * 2013-06-12 2014-12-25 扶桑建設工業株式会社 Biological contact filtration apparatus

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