JP6651131B2 - Water collecting mechanism and gravity filtration pond equipped with the water collecting mechanism - Google Patents

Water collecting mechanism and gravity filtration pond equipped with the water collecting mechanism Download PDF

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JP6651131B2
JP6651131B2 JP2016071115A JP2016071115A JP6651131B2 JP 6651131 B2 JP6651131 B2 JP 6651131B2 JP 2016071115 A JP2016071115 A JP 2016071115A JP 2016071115 A JP2016071115 A JP 2016071115A JP 6651131 B2 JP6651131 B2 JP 6651131B2
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filtration
backwash
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清信 豊川
清信 豊川
裕司 ▲高▼橋
裕司 ▲高▼橋
健次 勝又
健次 勝又
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JFE Engineering Corp
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Description

本発明は、重力式ろ過池の集水機構及び該集水機構を備えた重力式ろ過池に関する。   The present invention relates to a water collection mechanism for a gravity filtration pond and a gravity filtration pond provided with the water collection mechanism.

浄水場では河川や貯水池などの水源から原水を取水し、浄化処理を施して水道水として一般の需要に供給している。前記浄化処理の方式としては急速ろ過方式が広く採用されている(特許文献1参照)。   Water purification plants take raw water from water sources such as rivers and reservoirs, purify it, and supply it to general demand as tap water. As a method of the purification treatment, a rapid filtration method is widely used (see Patent Document 1).

急速ろ過方式とは、原水に凝集沈殿処理を施して懸濁質及びコロイド質を可能な限り沈殿池で除去した後に、急速ろ過池でろ過処理を施す方式をいう。急速ろ過池から排出された処理水は、殺菌処理されたのちに水道水として一般に供給される。   The rapid filtration system refers to a system in which raw water is subjected to a coagulation sedimentation treatment to remove suspended solids and colloids as much as possible in a sedimentation basin and then filtered in a rapid filtration basin. The treated water discharged from the rapid filtration pond is generally supplied as tap water after being sterilized.

急速ろ過方式としては次の二つのタイプが知られている。
(1)ろ過池をセクション分割板によって複数のろ過セクションに分割し、ろ過セクション毎に逆流洗浄を行うタイプ
(2)単数のろ過セクションにてろ過するタイプ(一般の重力式ろ過池)
図7(a)に基づいて、急速ろ過方式によって原水を浄化する急速ろ過池におけるろ過処理について説明する。原水渠1の原水は原水流入孔2を通ってろ過セクション3に流入し、ろ過セクション3内に配置されたろ材4を高速で通過することにより、原水中のフロック等の懸濁物質がろ材に付着されるか、ろ過層によってふるい分けされることにより除去される。ろ過された浄水は集水装置5を通過して浄水室6に流入し、浄水管7から浄水渠8に流出する。
The following two types are known as rapid filtration systems.
(1) A type in which a filtration pond is divided into a plurality of filtration sections by a section dividing plate, and backflow washing is performed for each filtration section. (2) A type in which filtration is performed in a single filtration section (general gravity type filtration pond)
Based on FIG. 7A, a description will be given of a filtration process in a rapid filtration pond for purifying raw water by a rapid filtration method. Raw water from the raw culvert 1 flows into the filtration section 3 through the raw water inflow hole 2 and passes through the filter medium 4 arranged in the filtration section 3 at high speed, so that suspended substances such as flocs in the raw water flow into the filter medium. Attached or removed by sieving through a filtration layer. The filtered purified water passes through the water collecting device 5, flows into the water purification chamber 6, and flows out of the water purification pipe 7 to the water purifier 8.

ろ過処理を継続すると、原水から除去された懸濁物質がろ材4に堆積してろ材間で目詰まりが生じ、急速ろ過池におけるろ過処理能力は低下する。ろ過処理能力が低下すると、ろ過処理を経たろ過水の濁度が上昇して水質が悪化したり、損失水頭が増加して必要とされるろ過流量を得ることが難しくなったりする。このため、間欠的にろ材4を洗浄してろ材4に堆積した懸濁物質を取り除く逆流洗浄によってろ材4を再生させる必要がある。   If the filtration process is continued, suspended matter removed from the raw water accumulates on the filter media 4 and clogging occurs between the filter media, and the filtration capacity of the rapid filtration pond decreases. When the filtration capacity is reduced, the turbidity of the filtered water increases and the water quality deteriorates, or the head loss increases and it becomes difficult to obtain a required filtration flow rate. For this reason, it is necessary to regenerate the filter medium 4 by backwashing in which the filter medium 4 is intermittently washed to remove suspended substances deposited on the filter medium 4.

そして、複数セクションに分かれたろ過池の場合、一つのろ過セクションを洗浄してろ材層の堆積物(フロック)を除去すると、当該ろ過セクションのろ過抵抗が無くなり、ろ過流速が増加する。そうすると、原水が十分ろ過できないままろ材を通過したり、洗浄直後にろ材層中に軽く捕捉(抑留)されているフロックが流出してきて、浄水の水質悪化の原因となる。   In the case of a filtration pond divided into a plurality of sections, when one filtration section is washed to remove deposits (flock) of the filter medium layer, the filtration resistance of the filtration section disappears and the filtration flow rate increases. Then, the raw water passes through the filter medium without being sufficiently filtered, or the flocs that are lightly captured (retained) in the filter medium layer immediately after the washing flow out, resulting in deterioration of the quality of purified water.

そこで、複数セクションに分かれたろ過池の場合、従来は、ろ過セクションの最終出口である浄水管7に、流速を増加させないために図7(b)、(c)、(d)に示すような流速調整機構60を設けている。流速調整機構60は、フラップ弁形状の邪魔板61に小口径の通水穴64を有するものであり、邪魔板61はヒンジ63によって支持板62に開閉自在に取付けられている。この邪魔板61はろ過時にはろ過抵抗体として作用する。
邪魔板61は、ろ過時は小口径の通水穴64を通じて浄水が流出し、逆洗時には図6(c)に示すように逆洗水流によりはねあがり、少ない抵抗で多量の逆洗水を通水することができる。
しかしながら、邪魔板には逆洗時に逆洗水が直接吹き付けるため、邪魔板のヒンジ63が損傷し易く、数年で邪魔板が欠落することがあった。また、邪魔板が水流の妨げ(乱れの原因)となり、ろ過砂の均一な洗浄に悪影響を及ぼすという問題があった。
また、単数個のろ過セクションを有する一般の重力式ろ過池においては、ろ過池の平面について見たとき異なる箇所においてろ過速度および逆洗速度にばらつきが生じるという問題があった。
Therefore, in the case of a filtration pond divided into a plurality of sections, conventionally, as shown in FIGS. 7 (b), (c), and (d), in order to prevent the flow rate from increasing in the water purification pipe 7, which is the final outlet of the filtration section. A flow rate adjusting mechanism 60 is provided. The flow rate adjusting mechanism 60 has a small-diameter water passage hole 64 in a flap valve-shaped baffle plate 61, and the baffle plate 61 is attached to a support plate 62 by a hinge 63 so as to be freely opened and closed. This baffle plate 61 acts as a filtration resistor during filtration.
The baffle plate 61 discharges purified water through a small-diameter water passage hole 64 during filtration, and rebounds by a backwashing water flow as shown in FIG. 6C during backwashing, and removes a large amount of backwash water with a small resistance. Water can be passed.
However, since backwash water is directly sprayed on the baffle plate at the time of backwashing, the hinge 63 of the baffle plate is easily damaged, and the baffle plate may be missing in several years. Further, there is a problem that the baffle plate hinders the flow of water (causes turbulence) and adversely affects the uniform cleaning of the filtered sand.
Further, in a general gravity filter having a single filtration section, there is a problem that the filtration speed and the backwash speed vary at different locations when viewed on the plane of the filter.

特開2003−299911号公報JP-A-2003-299911

本発明は、ろ過池の異なる箇所におけるろ過速度および逆洗速度のバラツキをなくすことを目的とする。
より詳細には、本発明は、ろ過池が複数のろ過セクションに区分にされている重力式ろ過池において、邪魔板61を設けることなく、一つのろ過セクションを逆洗した直後でも、当該ろ過セクションにおけるろ過流速が増加しないようにした集水機構を提供することを目的とする。
また、本発明は、単数個のろ過セクションを有する重力式ろ過池において、ろ過速度および逆洗速度を均一にする(ろ過池平面で見たとき異なる箇所におけるろ過速度および逆洗速度のばらつきを抑える)ことを目的とする。
An object of the present invention is to eliminate variations in filtration speed and backwash speed at different locations in a filtration pond.
More specifically, the present invention relates to a gravity-type filtration pond in which the filtration basin is divided into a plurality of filtration sections, without providing the baffle plate 61, even immediately after backwashing one filtration section, It is an object of the present invention to provide a water collecting mechanism that prevents a filtration flow rate from increasing.
In addition, the present invention makes the filtration speed and the backwashing speed uniform in a gravity filtration pond having a single filtration section (suppresses the dispersion of the filtration speed and the backwashing speed at different points when viewed in the plane of the filtration pond). ).

上記課題を解決するための本発明は以下に記載する通りのものである。
(1)原水渠と、
ろ材層を有し被処理水のろ過処理を行うろ過セクションと、
前記ろ過セクションで得られた浄水を貯蔵する浄水渠と、
を含む重力式ろ過池において用いられ、
前記ろ過セクション内に設けられた集水機構であって、
該集水機構は、ろ材を支持すると共にろ過空間を上下に区分する集水装置と、該集水装置の下方に設けられた流速調整機構とを含み、
前記流速調整機構は、複数の逆洗孔を有する穿孔板と、穿孔板の上流側において逆洗孔を塞ぐ部材とを備えており、前記逆洗孔を塞ぐ部材は、ろ過時には前記逆洗孔を塞いでろ過水の流路面積を狭めて前記逆洗孔を通過する過水の流水量を減少させるように作用し、逆洗時には前記逆洗孔を開放して逆洗水の流路面積を広げ、前記逆洗孔を通過する逆洗水の流水量を増大させて洗浄に必要な水量を確保するように作用する部材であることを特徴とする集水機構。
(2)前記流速調整機構が、複数の逆洗孔を有する穿孔板と、
ろ過水が通過するための通水孔を有し、かつ前記逆洗孔よりも大径の弁体と、からなり、
前記弁体は前記穿孔板の上流側において前記逆洗孔を塞ぐようにして弁体の端部が穿孔板に固定されていることを特徴とする上記(1)に記載の集水機構。
(3)前記流速調整機構が、複数の逆洗孔を有する穿孔板と、
長尺状のバンド体又はシート体と、からなり、
前記バンド体又はシート体は、前記穿孔板の上流側において前記複数個の逆洗孔を塞ぐように前記穿孔板に固定され、前記複数個の逆洗孔のそれぞれに対応する位置にろ過水が通過するための通水孔を有していることを特徴とする上記(1)に記載の集水機構。
(4)前記流速調整機構が、複数の逆洗孔を有する穿孔板と、
ボールと、からなり、
前記ボールは前記逆洗孔の上流側において、逆洗孔を形成している穿孔板の壁とボールとの間にろ過水の流路空間が形成されるように穿孔板に半固定されている
ことを特徴とする上記(1)に記載の集水機構。
(5)原水渠と、
ろ材層を有し被処理水のろ過処理を行うろ過セクションと、
前記ろ過セクションで得られた浄水を貯蔵する浄水渠と、
を含む重力式ろ過池であって、上記(1)〜(4)のいずれかに記載の集水機構を備えたことを特徴とする重力式ろ過池。
(6)前記ろ過セクションを単数個有することを特徴とする上記(5)に記載の重力式ろ過池。
(7)前記ろ過セクションを複数個有し、ろ過セクションをセクション毎に移動して逆流洗浄する逆流洗浄装置を備えたことを特徴とする上記(5)に記載の重力式ろ過池。
The present invention for solving the above problems is as described below.
(1) The original culvert,
A filtration section having a filter medium layer and performing a filtration treatment of the water to be treated,
A water purifier for storing purified water obtained in the filtration section,
Used in gravity filtration ponds containing
A water collecting mechanism provided in the filtration section,
The water collecting mechanism includes a water collecting device that supports a filter medium and divides a filtering space into upper and lower portions, and a flow rate adjusting mechanism provided below the water collecting device,
The flow rate adjustment mechanism includes a perforated plate having a plurality of backwash hole, and a member for closing the backwash holes upstream of the perforated plate, member for closing the backwash holes, wherein the filtration Gyakuaraiana the closed by narrowing the flow passage area of the filtered water acts to reduce the water flow of filtration water through the backwash hole, the flow path of the backwash water by opening the backwashing pores during backwashing spread area, catchment mechanism, characterized in that said a member acting to backwash holes to increase the water flow of backwash water to pass through the securing the amount of water required for cleaning.
(2) a perforated plate having a plurality of backwash holes, wherein the flow rate adjusting mechanism comprises:
Having a water hole for filtered water to pass through, and a valve body having a larger diameter than the backwash hole,
The water collecting mechanism according to (1), wherein the valve body has an end portion fixed to the perforated plate so as to close the backwash hole on an upstream side of the perforated plate.
(3) a perforated plate having a plurality of backwash holes, wherein the flow rate adjusting mechanism comprises:
Consisting of a long band or sheet,
The band body or the sheet body is fixed to the perforated plate so as to cover the plurality of backwash holes on the upstream side of the perforated plate, and filtered water is provided at a position corresponding to each of the plurality of backwash holes. The water collecting mechanism according to the above (1), wherein the water collecting mechanism has a water passage hole for passing therethrough.
(4) a perforated plate having a plurality of backwash holes;
Consisting of a ball and
The ball is semi-fixed to the perforated plate so that a flow path space for filtered water is formed between the ball and the wall of the perforated plate forming the backwash hole on the upstream side of the backwash hole. The water collecting mechanism according to (1), wherein:
(5) Raw culvert,
A filtration section having a filter medium layer and performing a filtration treatment of the water to be treated,
A water purifier for storing purified water obtained in the filtration section,
And a gravity filter provided with the water collecting mechanism according to any one of the above (1) to (4).
(6) The gravity filtration pond according to the above (5), wherein the filtration section has a single filtration section.
(7) The gravity type filtration pond according to the above (5), further comprising a backflow washing device having a plurality of the filtration sections and performing backflow washing by moving the filtration sections for each section.

本発明における集水機構を採用することにより、ろ過セクションの異なる箇所におけるろ過速度が均一化されるので、ろ過速度が特定の箇所で速くなることがない。このため、原水が十分ろ過できないままろ材を通過したり、洗浄直後にろ材層中に軽く捕捉(抑留)されているフロックが流出することがなく、浄水の水質悪化を防ぐことができる。また、逆洗時にはろ過セクションの異なる箇所における逆洗速度が均一化され、均等な洗浄が可能となる。   By adopting the water collecting mechanism in the present invention, the filtration speed at different locations in the filtration section is made uniform, so that the filtration speed does not increase at a specific location. For this reason, the raw water does not pass through the filter medium without being sufficiently filtered, and the flocs that are lightly captured (retained) in the filter medium layer immediately after washing do not flow out, so that the water quality of purified water can be prevented from deteriorating. In addition, at the time of backwashing, the backwashing speed at different portions of the filtration section is made uniform, and uniform washing becomes possible.

逆流洗浄装置移動型ろ過装置の概要を示す図である。(a)は逆流洗浄装置移動型ろ過装置の平面図であり、(b)は(a)のA−A’断面図である。It is a figure which shows the outline of a backwash washing | cleaning apparatus mobile filtration device. (A) is a top view of a backflow washing | cleaning apparatus mobile filtration device, (b) is A-A 'sectional drawing of (a). 本発明に係る実施形態のろ過装置のろ過時及び逆流洗浄時の状態を示す図である。It is a figure which shows the state at the time of filtration of the filtration apparatus of embodiment which concerns on this invention, and backwashing. 本発明の実施形態に係る流速調整機構の構造を示す図である。It is a figure showing the structure of the flow velocity adjusting mechanism concerning the embodiment of the present invention. 図3に示した流速調整機構において用いる弁体の平面構造を示す図である。FIG. 4 is a diagram illustrating a planar structure of a valve body used in the flow rate adjusting mechanism illustrated in FIG. 3. 本発明の実施形態に係る、図3と別構造の流速調整機構の構造を示す図である。FIG. 4 is a diagram illustrating a structure of a flow rate adjusting mechanism having a structure different from that of FIG. 3 according to the embodiment of the present invention. 本発明の実施形態に係る、図3、4と別構造の流速調整機構の構造を示す図である。FIG. 5 is a diagram illustrating a structure of a flow rate adjusting mechanism having a structure different from that of FIGS. 3 and 4 according to the embodiment of the present invention. 従来の逆流洗浄装置移動型ろ過装置の構造を示す図である。It is a figure which shows the structure of the conventional backflow washing | cleaning apparatus mobile filtration device.

以下では、本発明の集水機構を複数個のろ過セクションを有する逆流洗浄装置移動型の重力式ろ過池に適用した場合を例にとって述べる。
まず、本発明に係る重力式ろ過池の構成の一例を図1(a)、図1(b)に基づいて説明する。
図1(a)はろ過池の平面図であり、ろ過装置100のろ過池はセクション分割板15によって複数のろ過セクション3に分割されている。
図1(b)は図1(a)のA−A’断面図であり、一つの区画について逆流洗浄(以下、「逆洗」ともいう)を行っている状態を示している。
In the following, a case where the water collecting mechanism of the present invention is applied to a gravity filter of a backflow washing device moving type having a plurality of filtration sections will be described as an example.
First, an example of the configuration of the gravity filtration pond according to the present invention will be described with reference to FIGS. 1 (a) and 1 (b).
FIG. 1A is a plan view of the filtration pond. The filtration pond of the filtration device 100 is divided into a plurality of filtration sections 3 by a section dividing plate 15.
FIG. 1B is a cross-sectional view taken along the line AA ′ of FIG. 1A, and shows a state where backflow cleaning (hereinafter, also referred to as “backwashing”) is performed for one section.

本発明の実施形態に係るろ過装置について以下説明する。
(ろ過工程)
原水は、原水渠1より原水流入孔2によって均等にろ過セクション3に流入する。
ろ過セクション3内には集水装置5の上にろ材4が堆積している。原水はろ材4を通過して懸濁質を除去されて浄水となり、集水装置5、浄水室6及び浄水管7を経て浄水渠8に流出する。
Hereinafter, a filtration device according to an embodiment of the present invention will be described.
(Filtration process)
Raw water flows into the filtration section 3 from the raw culvert 1 uniformly through the raw water inlet 2.
In the filtration section 3, a filter medium 4 is deposited on a water collecting device 5. The raw water passes through the filter medium 4 to remove suspended solids, becomes purified water, and flows out to the water purifier 8 through the water collecting device 5, the water purifying room 6, and the water purifying pipe 7.

(逆流洗浄工程)
逆流洗浄装置20は電動式の走行台21、逆流洗浄ポンプ22 、表面洗浄ポンプ23、排水ポンプ24、クリーナーボックス25、駆動装置26及び制御盤27によって構成されている。
ろ過セクション3に逆流洗浄の必要が生じたとき、走行台21がろ過池の任意のろ過セクション3の真上で停止し、逆流洗浄ポンプ22が稼働して浄水渠8内の浄水を逆流洗浄水及び表面洗浄水として送出する。浄水は逆流洗浄ポンプ22で加圧され、一部は逆洗管を経て表面洗浄ポンプ23でさらに加圧されて表面洗浄水として使用され、一部は浄水渠8の下部より浄水管7を逆流して逆流洗浄水として使用される。ろ材4を洗浄した排水は、排水ポンプ24によって集水され、排水とい12に排出されて排水ます13に流入する。
(Backwashing process)
The backflow cleaning device 20 includes an electric traveling platform 21, a backflow cleaning pump 22, a surface cleaning pump 23, a drainage pump 24, a cleaner box 25, a driving device 26, and a control panel 27.
When the backwashing of the filtration section 3 becomes necessary, the carriage 21 stops immediately above any of the filtration sections 3 in the filtration pond, and the backwashing pump 22 operates so that the purified water in the water purifier 8 is backwashed. And discharged as surface cleaning water. The purified water is pressurized by a backwashing pump 22, a part thereof is further pressurized by a surface washing pump 23 through a backwashing pipe and used as surface washing water, and a part of the purified water flows back through the purified water pipe 7 from the lower part of the water purifier 8. And used as backwash water. The wastewater from which the filter medium 4 has been washed is collected by a drainage pump 24, discharged to a drainage ladle 12 and flows into a drainage drain 13.

逆洗前と逆洗後のろ過層の状態を図2に基づいて説明する。
図2(a)は逆洗前の状態を示し、図2(b)は逆洗後の状態を示す。
逆洗前は、図2(a)に示すように、原水Wはセクション分割板15によって分割された各セクションのろ過層4を通って浄化され集水装置5を経て浄水室6に流入する。この時、いずれのろ過層においてもろ過抵抗に大きな差異はなく、ろ過速度29にも大きな差異はない。
しかしながら、一つのろ過セクションを逆洗した直後、図2(b)に示すように当該ろ過セクションの堆積物(フロック)28が除去されて、当該ろ過セクションのみろ過抵抗が小さくなるためろ過速度29’が増大する。
The state of the filtration layer before and after backwashing will be described with reference to FIG.
FIG. 2A shows a state before backwashing, and FIG. 2B shows a state after backwashing.
Before backwashing, as shown in FIG. 2A, the raw water W is purified through the filtration layer 4 of each section divided by the section dividing plate 15 and flows into the water purification chamber 6 via the water collecting device 5. At this time, there is no large difference in the filtration resistance in any of the filtration layers, and there is no large difference in the filtration speed 29.
However, immediately after backwashing one filtration section, as shown in FIG. 2 (b), the sediment (flock) 28 of the filtration section is removed, and only the filtration section has a reduced filtration resistance. Increase.

そこで、本発明においては集水装置の下方に流速調整機構(ろ過抵抗体)を配置することによって流速の増加を抑える。
以下では流速調整機構の実施形態について説明する。
Therefore, in the present invention, an increase in flow velocity is suppressed by disposing a flow velocity adjusting mechanism (filtering resistor) below the water collecting device.
Hereinafter, an embodiment of the flow rate adjusting mechanism will be described.

(実施形態1)
図3、図4は流速調整機構の実施形態の構造を示す図である。
流速調整機構30は集水装置5の下方に配置される。
なお、集水装置5は、ろ過区画を上部空間と下部空間とに分割する床板として設けられ、多孔板または複数の集水ノズル付の仕切板からなるものが一般的であるが、図3では図示を省略する。
(Embodiment 1)
3 and 4 are views showing the structure of the embodiment of the flow rate adjusting mechanism.
The flow velocity adjusting mechanism 30 is disposed below the water collecting device 5.
In addition, the water collecting device 5 is provided as a floor plate that divides a filtration section into an upper space and a lower space, and generally includes a perforated plate or a partition plate with a plurality of water collecting nozzles. Illustration is omitted.

流速調整機構30は所定の間隔を置いて複数の逆洗孔32を設けた穿孔板31とこの穿孔板31の逆洗孔32を塞ぐように設けられた弁体33とからなる。この弁体33はその端部の支持部35によって前記穿孔板31に固定されており、逆洗水の水流によってこの支持部35を支点として上方に向かって回転運動をする(開く)ことができるようになっている。
ろ過時においては弁体33はろ過水の水流および自重等によって穿孔板31に押しつけられているため、ろ過水は通水孔34で流速を抑えられて浄水室に流入する。このとき、通水孔34は小径であるため、弁体33はろ過水に対してろ過抵抗体として作用する。
一方、逆洗時においては、弁体33は逆洗水の水流によって、図3に示すように支持部35を支点として回転する(開く)ことにより、逆洗水の流路面積が広がり、逆洗に必要な水量を確保できる。
The flow rate adjusting mechanism 30 includes a perforated plate 31 provided with a plurality of backwash holes 32 at predetermined intervals, and a valve body 33 provided to close the backwash holes 32 of the perforated plate 31. The valve body 33 is fixed to the perforated plate 31 by a support portion 35 at an end thereof, and can be rotated upward (opened) with the support portion 35 as a fulcrum by the backwash water flow. It has become.
During filtration, the valve element 33 is pressed against the perforated plate 31 by the flow of the filtered water and its own weight, etc., so that the filtered water flows into the water purification chamber at a reduced flow rate through the water passage holes 34. At this time, since the water hole 34 has a small diameter, the valve body 33 acts as a filtration resistor against the filtered water.
On the other hand, at the time of backwashing, the valve body 33 rotates (opens) about the support portion 35 as a fulcrum as shown in FIG. The amount of water required for washing can be secured.

図4は弁体33の一例の平面図である。
弁体33は逆洗孔32よりも径が大きくなっている。弁体33の中央部にはろ過水の通水孔34が設けられており、弁体33は支持部35において押さえ部材36によって穿孔板に固定される。
FIG. 4 is a plan view of an example of the valve element 33.
The valve body 33 has a larger diameter than the backwash hole 32. A water hole 34 for filtered water is provided at the center of the valve body 33, and the valve body 33 is fixed to a perforated plate by a holding member 36 at a support portion 35.

(実施形態2)
図5に異なる実施形態の流速調整機構40の例を示す。
本実施形態の流速調整機構40は長尺上の可撓性のあるバンド体41に複数の通水孔42を設けたものである。バンド41は、図3に示したような所定間隔をおいて逆洗孔32が穿たれている穿孔板31に押さえ部材43によって固定される。
ろ過時において、バンド体41はろ過水の水流および自重等によって穿孔板31に押しつけられているため、ろ過水は通水孔42で流速を抑えられて浄水室に流入する。このとき、通水孔42は小径であるため、ろ過水に対してろ過抵抗体として作用する。
一方、逆洗時においては、可撓性のあるバンド体41は逆洗水の水流によって、押さえ部材43以外のバンド体41が浮く(開く)ことにより、逆洗水の流路面積が広がり、逆洗に必要な水量を確保できる。
(Embodiment 2)
FIG. 5 shows an example of a flow rate adjusting mechanism 40 according to a different embodiment.
The flow velocity adjusting mechanism 40 according to the present embodiment has a long flexible band member 41 provided with a plurality of water passage holes 42. The band 41 is fixed to the perforated plate 31 in which the backwash holes 32 are formed at predetermined intervals as shown in FIG.
At the time of filtration, since the band body 41 is pressed against the perforated plate 31 by the flow of the filtered water and its own weight or the like, the filtered water flows into the water purification chamber at a reduced flow rate through the water holes 42. At this time, since the water passage hole 42 has a small diameter, it acts as a filtration resistor against the filtered water.
On the other hand, at the time of backwashing, the band body 41 other than the pressing member 43 floats (opens) due to the water flow of the backwash water in the flexible band body 41, thereby increasing the flow area of the backwash water. The amount of water required for backwashing can be secured.

また、バンド体41を複数並列に配置する場合、前記のように流速調整機構をバンド形状とすることに代えて、穿孔板31の全面を覆う全面シート型としてもよい。全面シート型のところどころにスリット(切れ目)を有した形状、つまり、複数のバンド体41が部分的に連結した形状である。逆洗時においては、可とう性のあるシートは逆洗水の水流によって、押さえ部材43以外のシートが浮き、シートのスリットが開くことで流路面積が広がり、逆洗に必要な水量を確保できる。   When a plurality of band members 41 are arranged in parallel, instead of forming the flow velocity adjusting mechanism in a band shape as described above, a full sheet type covering the entire surface of the perforated plate 31 may be used. This is a shape having slits (cuts) in some places of the full sheet type, that is, a shape in which a plurality of band bodies 41 are partially connected. At the time of backwashing, the flexible sheet is floated by the backwashing water flow, so that the sheets other than the pressing member 43 are floated, and the slits of the sheet are opened, so that the flow path area is widened and the amount of water necessary for backwashing is secured. it can.

(実施形態3)
図6に基づいて本実施形態について説明する。
図6において、流速調整機構50は通水孔52を有する穿孔板51と、通水孔52の上流側に支持部材54に重力によって穿孔板51に半固定されたボール53とからなっている(穿孔板51と支持部材54は一体でも良い)。
ボール53と穿孔板51との間の空間がろ過水の流路55を形成している。
この流路55の流路断面積は小さく形成されているため、この流路55のろ過抵抗が大きく、逆洗直後においてもろ過水の流速が増大することがない。
一方、逆洗時には逆洗水の水圧を受けボール50が浮上し、穿孔板51との隙間が広がり、逆洗水に対して抵抗体として作用せず、逆洗に必要な流量を確保することができる。
ボール53の材質としては樹脂、樹脂と金属との複合材料又はセラミックが好ましい。
さらに、ボール50は穿孔板51又は支持部材54に対して伸び縮みするような樹脂材料で固定されているのが好ましい。
(Embodiment 3)
This embodiment will be described with reference to FIG.
In FIG. 6, the flow rate adjusting mechanism 50 includes a perforated plate 51 having a water passage hole 52 and a ball 53 that is semi-fixed to the perforated plate 51 by gravity on the support member 54 on the upstream side of the water passage hole 52 (see FIG. 6). The perforated plate 51 and the support member 54 may be integrated.)
The space between the ball 53 and the perforated plate 51 forms a flow path 55 of the filtered water.
Since the cross-sectional area of the flow channel 55 is formed small, the filtration resistance of the flow channel 55 is large, and the flow rate of the filtered water does not increase even immediately after backwashing.
On the other hand, at the time of backwashing, the ball 50 rises due to the water pressure of the backwashing water, the gap with the perforated plate 51 is widened, and it does not act as a resistor against the backwashing water, and secures a flow rate necessary for backwashing. Can be.
The material of the ball 53 is preferably a resin, a composite material of a resin and a metal, or a ceramic.
Further, the ball 50 is preferably fixed with a resin material that expands and contracts with respect to the perforated plate 51 or the support member 54.

上記のように、流速調整機構30、40、50が集水装置5の下方に配置されており、小さい流速調整機構が多数存在し逆洗時の衝撃力を減少させるため、従来の流速調整部材(ヒンジおよび邪魔板)のような損傷が生じにくい。
また、本発明における流速調整機構30、40、50は通気の邪魔となることがないため、空洗洗浄兼用型としても製作可能である。
更に、逆流洗浄の均等化の効果もある 。
加えて、ろ過時において、圧力損失(抵抗体)となるものの、ろ過速度の均等化の効果も有する。
As described above, the flow rate adjusting mechanisms 30, 40, and 50 are disposed below the water collecting device 5, and there are many small flow rate adjusting mechanisms to reduce the impact force during backwashing. (Hinges and baffles) are less likely to occur.
Further, since the flow rate adjusting mechanisms 30, 40, and 50 in the present invention do not obstruct the ventilation, they can be manufactured as a type that is also used for both washing and cleaning.
Further, there is an effect of equalizing the backwashing.
In addition, at the time of filtration, a pressure loss (resistor) is produced, but it also has an effect of equalizing the filtration speed.

上記では本発明の集水機構を複数個のろ過セクションを有する重力式ろ過池に適用した場合について述べたが、本発明の集水機構を単数個のろ過セクションを有する重力式ろ過池に適用してもろ過速度の均一化という効果が奏されることは明らかである。   Although the case where the water collecting mechanism of the present invention is applied to a gravity filter having a plurality of filtration sections has been described above, the water collecting mechanism of the present invention is applied to a gravity filter having a single filter section. However, it is clear that the effect of making the filtration speed uniform can be obtained.

1 原水渠
2 原水流入孔
3 ろ過セクション(ろ過池の一区画)
4 ろ材、ろ過層
5 集水装置
6 浄水室
7 浄水管
8 浄水渠
9 逆洗摺動弁
10 浄水ます
11 浄水流出管
12 排水とい
13 排水ます
14 排水管
15 セクション分割板
20 逆流洗浄装置
21 走行台
22 逆流洗浄ポンプ
23 表面洗浄ポンプ(ろ過排水ポンプ)
24 排水ポンプ
25 クリーナーボックス
26 駆動装置
27 制御盤
28 堆積物
29、29’ ろ過速度
30、40、50 流速調整機構
31 穿孔板
32 逆洗孔
33 弁体
34 通水孔
35 支持部
36 押さえ部材
41 バンド体
42 通水穴
43 押さえ部材
51 穿孔板
52 通水孔
53 ボール
54 支持部材
55 通水路
60 流速調整機構
61 邪魔板
62 支持板
63 ヒンジ
64 通水穴
100 ろ過装置
1 Raw culvert 2 Raw water inlet 3 Filtration section (section of filtration pond)
Reference Signs List 4 filter media, filtration layer 5 water collecting device 6 water purification room 7 water purification tube 8 water purification conduit 9 backwash sliding valve 10 water purification masou 11 water purification outflow pipe 12 drainage drain 13 drainage 14 drainage pipe 15 section dividing plate 20 backflow cleaning device 21 traveling Table 22 Backflow cleaning pump 23 Surface cleaning pump (filtration drain pump)
DESCRIPTION OF SYMBOLS 24 Drain pump 25 Cleaner box 26 Drive device 27 Control panel 28 Deposit 29, 29 'Filtration speed 30, 40, 50 Flow rate adjusting mechanism 31 Perforated plate 32 Backwash hole 33 Valve body 34 Water passage hole 35 Supporting part 36 Pressing member 41 Band body 42 water passage hole 43 pressing member 51 perforated plate 52 water passage hole 53 ball 54 support member 55 water passage 60 flow rate adjusting mechanism 61 baffle plate 62 support plate 63 hinge 64 water passage hole 100 filtration device

Claims (7)

原水渠と、
ろ材層を有し被処理水のろ過処理を行うろ過セクションと、
前記ろ過セクションで得られた浄水を貯蔵する浄水渠と、
を含む重力式ろ過池において用いられ、
前記ろ過セクション内に設けられた集水機構であって、
該集水機構は、ろ材を支持すると共にろ過空間を上下に区分する集水装置と、該集水装置の下方に設けられた流速調整機構とを含み、
前記流速調整機構は、複数の逆洗孔を有する穿孔板と、穿孔板の上流側において逆洗孔を塞ぐ部材とを備えており、前記逆洗孔を塞ぐ部材は、ろ過時には前記逆洗孔を塞いでろ過水の流路面積を狭めて前記逆洗孔を通過する過水の流水量を減少させるように作用し、逆洗時には前記逆洗孔を開放して逆洗水の流路面積を広げ、前記逆洗孔を通過する逆洗水の流水量を増大させて洗浄に必要な水量を確保するように作用する部材であることを特徴とする集水機構。
Raw culvert,
A filtration section having a filter medium layer and performing a filtration treatment of the water to be treated,
A water purifier for storing purified water obtained in the filtration section,
Used in gravity filtration ponds containing
A water collecting mechanism provided in the filtration section,
The water collecting mechanism includes a water collecting device that supports a filter medium and divides a filtering space into upper and lower portions, and a flow rate adjusting mechanism provided below the water collecting device,
The flow rate adjustment mechanism includes a perforated plate having a plurality of backwash hole, and a member for closing the backwash holes upstream of the perforated plate, member for closing the backwash holes, wherein the filtration Gyakuaraiana the closed by narrowing the flow passage area of the filtered water acts to reduce the water flow of filtration water through the backwash hole, the flow path of the backwash water by opening the backwashing pores during backwashing spread area, catchment mechanism, characterized in that said a member acting to backwash holes to increase the water flow of backwash water to pass through the securing the amount of water required for cleaning.
前記流速調整機構が、複数の逆洗孔を有する穿孔板と、
ろ過水が通過するための通水孔を有し、かつ前記逆洗孔よりも大径の弁体と、からなり、
前記弁体は前記穿孔板の上流側において前記逆洗孔を塞ぐようにして弁体の端部が穿孔板に固定されていることを特徴とする請求項1に記載の集水機構。
The flow rate adjusting mechanism, a perforated plate having a plurality of backwash holes,
Having a water hole for filtered water to pass through, and a valve body having a larger diameter than the backwash hole,
2. The water collecting mechanism according to claim 1, wherein an end of the valve body is fixed to the perforated plate so as to close the backwash hole on an upstream side of the perforated plate. 3.
前記流速調整機構が、複数の逆洗孔を有する穿孔板と、
長尺状のバンド体又はシート体と、からなり、
前記バンド体又はシート体は、前記穿孔板の上流側において前記複数個の逆洗孔を塞ぐように前記穿孔板に固定され、前記複数個の逆洗孔のそれぞれに対応する位置にろ過水が通過するための通水孔を有していることを特徴とする請求項1に記載の集水機構。
The flow rate adjusting mechanism, a perforated plate having a plurality of backwash holes,
Consisting of a long band or sheet,
The band body or the sheet body is fixed to the perforated plate so as to cover the plurality of backwash holes on the upstream side of the perforated plate, and filtered water is provided at a position corresponding to each of the plurality of backwash holes. The water collecting mechanism according to claim 1, further comprising a water passage hole for passing the water collecting hole.
前記流速調整機構が、複数の逆洗孔を有する穿孔板と、
ボールと、からなり、
前記ボールは前記逆洗孔の上流側において、逆洗孔を形成している穿孔板の壁とボールとの間にろ過水の流路空間が形成されるように穿孔板に半固定されている
ことを特徴とする請求項1に記載の集水機構。
The flow rate adjusting mechanism, a perforated plate having a plurality of backwash holes,
Consisting of a ball and
The ball is semi-fixed to the perforated plate so that a flow path space for filtered water is formed between the ball and the wall of the perforated plate forming the backwash hole on the upstream side of the backwash hole. The water collecting mechanism according to claim 1, wherein:
原水渠と、
ろ材層を有し被処理水のろ過処理を行うろ過セクションと、
前記ろ過セクションで得られた浄水を貯蔵する浄水渠と、
を含む重力式ろ過池であって、請求項1〜4のいずれかに記載の集水機構を備えたことを特徴とする重力式ろ過池。
Raw culvert,
A filtration section having a filter medium layer and performing a filtration treatment of the water to be treated,
A water purifier for storing purified water obtained in the filtration section,
A gravity type filtration pond comprising the water collecting mechanism according to any one of claims 1 to 4.
前記ろ過セクションを単数個有することを特徴とする請求項5に記載の重力式ろ過池。   The gravity filtration pond according to claim 5, wherein the filtration section has a single filtration section. 前記ろ過セクションを複数個有し、ろ過セクションをセクション毎に移動して逆流洗浄する逆流洗浄装置を備えたことを特徴とする請求項5に記載の重力式ろ過池。   The gravity type filtration pond according to claim 5, comprising a plurality of the filtration sections, and a backwashing device for performing backflow washing by moving the filtration sections for each section.
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