JPS6022964Y2 - gravity filtration device - Google Patents

gravity filtration device

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Publication number
JPS6022964Y2
JPS6022964Y2 JP11670681U JP11670681U JPS6022964Y2 JP S6022964 Y2 JPS6022964 Y2 JP S6022964Y2 JP 11670681 U JP11670681 U JP 11670681U JP 11670681 U JP11670681 U JP 11670681U JP S6022964 Y2 JPS6022964 Y2 JP S6022964Y2
Authority
JP
Japan
Prior art keywords
water
drain
valve
pipe
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
Application number
JP11670681U
Other languages
Japanese (ja)
Other versions
JPS5823608U (en
Inventor
寛 本橋
Original Assignee
荏原インフイルコ株式会社
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 荏原インフイルコ株式会社 filed Critical 荏原インフイルコ株式会社
Priority to JP11670681U priority Critical patent/JPS6022964Y2/en
Publication of JPS5823608U publication Critical patent/JPS5823608U/en
Application granted granted Critical
Publication of JPS6022964Y2 publication Critical patent/JPS6022964Y2/en
Expired legal-status Critical Current

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Description

【考案の詳細な説明】 本考案は、上水、工業用水、その他の用水を濾過浄化す
るために空気洗浄を行なう重力式濾過装置の改良に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement of a gravity filtration device that performs air cleaning to filter and purify tap water, industrial water, and other water.

通常、空気洗浄を行なう重力式濾過槽においては、炉材
層の空気洗浄に先立って、あらかじめ槽内水位に逆洗排
水樋の上端よりも十分に下げておかないと、導入空気に
より水面が膨張し、流動状態の炉材が逆洗排水樋中に流
出して炉材の損失をきたす欠点がある。
Normally, in a gravity-type filtration tank that performs air cleaning, the water level in the tank must be lowered sufficiently below the top of the backwash drain gutter before cleaning the air in the furnace material layer, otherwise the introduced air will cause the water surface to expand. However, there is a drawback that the furnace material in a fluid state flows out into the backwash drainage gutter, causing loss of the furnace material.

従来ではそのため空気洗浄には機械的、電気制御装置を
付属させて特別な操作を行なっているが、装置が高価で
取扱上にも不便な問題点が多かった。
Conventionally, for this purpose, special operations have been carried out by attaching mechanical and electrical control devices to air cleaning, but these devices are expensive and have many problems in terms of handling.

本考案は、これら従来の諸欠点を適確に除去しようとす
るもので、炉材の空気洗浄に際し、何ら機械的、電気制
御を用いず、しかも特別の操作を行なうことなく所定の
水位まで水位を降下させ、炉材の流出を適確に防止する
ことができる装置を提供することを目的とするものであ
る。
The present invention aims to accurately eliminate these conventional drawbacks, and allows the water level to reach a predetermined level without using any mechanical or electrical control or special operations when cleaning the air of furnace materials. The object of the present invention is to provide a device that can lower the furnace material and accurately prevent the outflow of the furnace material.

本考案は、空気洗浄機構を備えた重力式濾過槽において
、該槽内を仕切壁にて濾過室と排水渠とに区画し、前記
濾過室に炉材層とその下方部に集水室を備え、前記炉材
層の上方部に逆洗排水樋を配設すると共に該逆洗排水樋
と炉材層との間に中間排水管を設け、前記逆洗排水樋を
前記仕切壁を介して前記排水渠に開口連通させ、さらに
前記集水室と濾過水流出渠とをサイフオンブレーカ−を
付設したサイフオン形成管にて連通させたことを特徴と
するものである。
The present invention is a gravity-type filtration tank equipped with an air cleaning mechanism, in which the tank is divided into a filtration chamber and a drain by a partition wall, and a furnace material layer is provided in the filtration chamber and a water collection chamber is provided below the filtration chamber. A backwash drain gutter is provided above the furnace material layer, and an intermediate drain pipe is provided between the backwash drain gutter and the furnace material layer, and the backwash drain gutter is connected to the furnace material layer through the partition wall. The present invention is characterized in that an opening communicates with the drain, and further, the water collection chamber and the filtered water outflow drain are communicated through a siphon-forming pipe equipped with a siphon breaker.

本考案の一実施例を図面について説明すれば、第1図に
おいて重力式濾過槽体1内は仕切壁2によって濾過室3
と排水渠4に仕切られ、この濾過室3の底部近くには通
水隔板5、例えば多孔板或いは網状部材が設けられてそ
の下部に集水室6が区画形成され、かつ通水隔板5の上
部には支持材とアンスラサイト、砂その他の濾過材とか
らなる炉材層7が備えられ、さらにその上方には逆洗排
水樋8が設けられている。
To explain one embodiment of the present invention with reference to the drawings, in FIG.
The filtration chamber 3 is partitioned into a drainage channel 4, and near the bottom of the filtration chamber 3, a water flow partition 5, such as a perforated plate or a net-like member, is provided, and a water collection chamber 6 is defined below the water flow partition 5. A furnace material layer 7 made of a supporting material and anthracite, sand, or other filtering material is provided on the upper part of the filter 5, and a backwash drainage gutter 8 is provided above the furnace material layer 7.

該逆洗排水樋8の一端は仕切壁2を介して排水渠4に開
口されていると共に、この逆洗排水樋8゛と炉材層7と
の間に中間排水弁19を備えた中間排水管15が配設さ
れている。
One end of the backwash drain gutter 8 is opened to the drain culvert 4 through the partition wall 2, and an intermediate drain valve 19 is provided between the backwash drain gutter 8' and the furnace material layer 7. A tube 15 is provided.

また、前記排水渠4の下部には洗浄排水弁20を付設し
た逆洗排水管16が接続され、前記集水室6には逆U字
型の濾過水流出管兼逆洗水管9(以、逆U字配管という
)、および空気洗浄弁21を付設した槽内空気洗浄管2
3が配設されている。
Further, a backwash drain pipe 16 equipped with a washing drain valve 20 is connected to the lower part of the drain 4, and the water collection chamber 6 is connected to an inverted U-shaped filtrate outflow pipe/backwash water pipe 9 (hereinafter referred to as (referred to as inverted U-shaped piping), and tank air cleaning pipe 2 equipped with an air cleaning valve 21
3 are arranged.

この前記逆U字配管9は流出渠22内の濾過水中に浸漬
され、その頂部には加圧空気供給用の空気流入弁11及
び大気開放弁12を付設した空気流出入管10が接続配
備され、さらに、槽体1の上方部には原水流入弁18を
付設した原水流入管14が接続されている。
The inverted U-shaped pipe 9 is immersed in filtered water in the outflow conduit 22, and an air inflow and outflow pipe 10 equipped with an air inflow valve 11 for supplying pressurized air and an atmosphere release valve 12 is connected to the top of the pipe 9, Further, a raw water inflow pipe 14 equipped with a raw water inflow valve 18 is connected to the upper part of the tank body 1 .

図中、13は流出堰、17は空気洗浄管、24.25,
26,27,28及び29は各弁の操作用シリンダで、
自動切替操作ができるようにタイマ或いは水位検知器な
どの検出信号で連動する制御システムにすることもでき
る。
In the figure, 13 is the outflow weir, 17 is the air cleaning pipe, 24.25,
26, 27, 28 and 29 are cylinders for operating each valve;
It is also possible to use a control system that is linked to a detection signal such as a timer or a water level detector so that automatic switching operation can be performed.

30は流入堰である。30 is an inflow weir.

次に、第1図乃至第3図によって上記実施例の操作要領
と作用を説明する。
Next, the operation procedure and operation of the above embodiment will be explained with reference to FIGS. 1 to 3.

(1) ’p通過程(第1図参照) 原水は原水流入管14、原水流入弁18、流入堰30を
経て槽体1内に導入され、炉材層7を下向きに通過する
間に原水中の濁質は炉材層7に捕捉され、濾過水は通水
隔板5を経て集水室6に至り、逆U字配管9を経て流出
渠22に流入し、流出堰13から外部に溢流する。
(1) 'P passage process (see Figure 1) Raw water is introduced into the tank body 1 through the raw water inlet pipe 14, raw water inlet valve 18, and inlet weir 30, and while passing downward through the furnace material layer 7, the raw water is Suspended matter in the water is captured in the furnace material layer 7, and the filtered water passes through the water flow partition plate 5, reaches the water collection chamber 6, flows into the outflow culvert 22 through the inverted U-shaped piping 9, and flows out from the outflow weir 13. overflow.

かかる濾過を継続するにしたがって炉材層7は捕捉濁質
によって抵抗を増すから槽体1内の水位は次第に上昇し
、ついに槽体1の上端近くに到達する。
As such filtration continues, the resistance of the furnace material layer 7 increases due to the trapped suspended solids, so the water level in the tank body 1 gradually rises and finally reaches near the top of the tank body 1.

このとき濾過操作を中止して前記炉材層7の逆洗を行な
う。
At this time, the filtration operation is stopped and the furnace material layer 7 is backwashed.

なお、この濾過操作中、大気開放弁12は開、閉いずれ
でもよいが、原水流入弁18以外はすべて閉にしておく
必要がある。
During this filtration operation, the atmosphere release valve 12 may be open or closed, but all valves other than the raw water inlet valve 18 must be closed.

(2)逆洗工程 (2)−1準備操作(第2図参照) 原水流入弁18を閉、中間排水弁19及び洗浄排水弁2
0を開として槽体1内の水位を降下させる。
(2) Backwash process (2)-1 Preparatory operations (see Figure 2) Close the raw water inlet valve 18, intermediate drain valve 19 and washing drain valve 2
0 and the water level in the tank body 1 is lowered.

この場合、濾過室3内の水位が中間排水管15の接続位
置近辺になるように、かつ流出渠22内の水位が変わら
ないように(流出渠22を満杯の状態に維持)すること
が大切であるが、そのために次のような弁開閉操作を行
なう。
In this case, it is important to keep the water level in the filtration chamber 3 close to the connection position of the intermediate drain pipe 15 and to keep the water level in the outflow conduit 22 unchanged (maintaining the outflow conduit 22 in a full state). However, for this purpose, the following valve opening and closing operations are performed.

すなわち、槽体1内の水位が流出渠22の水位(流出堰
13の高さ)Aに降下したときに(この間、流出渠22
は満杯のままである)、大気開放弁12を閉、空気流入
弁11を開として空気流入管10を通して逆U字配管9
内に加圧空気を導入することによって、流出渠22内の
濾過水が集水室6に逆流するのを予防する。
That is, when the water level in the tank body 1 falls to the water level A in the outflow culvert 22 (the height of the outflow weir 13) (during this period, the outflow culvert 22
(remains full), close the atmosphere release valve 12, open the air inflow valve 11, and pass the air inflow pipe 10 through the inverted U-shaped pipe 9.
By introducing pressurized air into the drain, the filtered water in the outflow conduit 22 is prevented from flowing back into the water collection chamber 6.

このとき、逆U字配管9内ではその濾過水硫入側配管9
′と濾過水硫出側配管9″とが一時的に等水位となるが
、前記逆流防止を完全なものとするためには第2図にお
いてH>h□であることが必要であると共に、H<h2
であることが好ましい(H>h2の場合、加圧空気が流
出渠22内に流出し、無駄に消費される)。
At this time, in the inverted U-shaped pipe 9, the filtered water sulfur input side pipe 9
' and the filtered water sulfur outlet pipe 9'' are temporarily at the same water level, but in order to completely prevent the backflow, it is necessary that H>h□ in Fig. 2, H<h2
(If H>h2, pressurized air flows out into the outflow conduit 22 and is wasted).

すなわち、加圧空気の圧力Pはp> (Po十ρht)
であることが必要であり、Pく(Po十ρh2)である
ことが望ましい。
That is, the pressure P of pressurized air is p> (Po×ρht)
It is necessary that the value be P, and it is desirable that the value be P×(Po×ρh2).

但し、Poは大気圧、ρは濾過水の密度である。However, Po is the atmospheric pressure and ρ is the density of the filtered water.

しかして、槽体1内の水位が更に降下し、濾過室3内の
水位が中間排水管15の接続位置すなわち水位Bになる
と当然該中間排水管15からの水の流出が止まるが、こ
の間に前記濾過水流入側配管9′内の水位は徐々に低下
し、第3図に示すように最終的には該水位と濾過室水位
Bとの差はHとなる。
However, when the water level in the tank body 1 further falls and the water level in the filtration chamber 3 reaches the connection position of the intermediate drain pipe 15, that is, water level B, the outflow of water from the intermediate drain pipe 15 naturally stops; The water level in the filtrate inlet pipe 9' gradually decreases, and eventually the difference between the water level and the filtration chamber water level B becomes H, as shown in FIG.

これは逆U字配管9内の加圧空気圧力が(po十pH)
であり、濾過室3内の水面に大気圧P。
This means that the pressurized air pressure inside the inverted U-shaped pipe 9 is (po + pH)
and atmospheric pressure P on the water surface in the filtration chamber 3.

が掛かつているからである。This is because it is on.

以上の操作においては、初めに大気開放弁12を閉、空
気流入弁11を開としたのちに原水流入弁18を閉、中
間排水弁19及び洗浄排水弁20を開としてもよい。
In the above operation, the atmosphere release valve 12 may be closed first, the air inflow valve 11 may be opened, the raw water inflow valve 18 may be closed, and the intermediate drain valve 19 and the cleaning drain valve 20 may be opened.

この場合、一時的に空気流入弁11の高さまで濾過水が
流入することがあるが全く問題はない。
In this case, the filtered water may temporarily flow up to the height of the air inflow valve 11, but this is not a problem at all.

なお、洗浄排水弁20は開のままにし、排水渠4内は空
にしてもよい。
Note that the cleaning drain valve 20 may be left open and the drain culvert 4 may be emptied.

(2)−2逆洗操作(第3図参照) 濾過室3内の水位がBに到達したらば中間排水弁19を
閉としたのち、空気洗浄弁21を開として槽内空気洗浄
管23から空気を導入すれば空気は通水隔板5を経て濾
過室3内を上昇し、炉材層7を流動攪拌して洗浄が行な
われる。
(2)-2 Backwash operation (see Figure 3) When the water level in the filtration chamber 3 reaches B, the intermediate drain valve 19 is closed, and the air cleaning valve 21 is opened to drain air from the tank air cleaning pipe 23. When air is introduced, the air rises in the filtration chamber 3 through the water flow partition plate 5, and the furnace material layer 7 is fluidly stirred and cleaned.

この空気洗浄中は導入空気によって水面は膨張するが、
すでに水面は逆洗排水樋8の上端より十分降下している
から膨張水面は逆洗排水樋8の上端には達せず、したが
って流動状態の炉材が逆洗排水樋8内に従来のように流
出することはない。
During this air cleaning, the water surface expands due to the introduced air, but
Since the water level has already fallen sufficiently below the upper end of the backwash drain gutter 8, the expanded water level does not reach the upper end of the backwash drain gutter 8, and therefore the furnace material in a fluid state is stored in the backwash drain gutter 8 as before. It will not leak out.

かかる空気洗浄を一定時間荷なったのち空気洗浄弁21
を閉にすると共に空気流入弁11を閉、大気開放弁12
を開として逆U字配管9内の加圧空気を大気中に放出す
れば、流出渠22内の濾過水がその水圧によって逆U字
配管9内を逆流して濾過室3内に流入し、該濾過水は通
水隔板5を経て上昇し、前記空気洗浄によって炉材から
剥離された濁質を浮遊させ、その排水は逆洗排水樋8か
ら排水渠4内に至り洗浄排水弁20から外部に排出され
能率よく逆洗操作ができる。
After this air cleaning has been carried out for a certain period of time, the air cleaning valve 21
and close the air inflow valve 11, and the atmosphere release valve 12.
When the pressurized air in the inverted U-shaped pipe 9 is released into the atmosphere by opening the inverted U-shaped pipe 9, the filtered water in the outflow conduit 22 flows back through the inverted U-shaped pipe 9 due to the water pressure and flows into the filtration chamber 3. The filtered water rises through the water flow partition plate 5 and suspends the suspended solids separated from the furnace material by the air washing, and the waste water flows from the backwash drain gutter 8 into the drain culvert 4 and from the wash drain valve 20. It is discharged outside, allowing for efficient backwashing.

なお、中間排水弁19を閉としたのち、空気洗浄弁21
を開、空気流入弁11を閉、大気開放弁12を開とする
ことにより水逆洗と空気逆洗を同時に行なうことができ
ることは上記説明から明らかであろう。
Note that after closing the intermediate drain valve 19, the air cleaning valve 21 is closed.
It will be clear from the above description that water backwashing and air backwashing can be performed simultaneously by opening the valve, closing the air inflow valve 11, and opening the atmosphere release valve 12.

(31p過工程再開 このようにして一定時間逆洗を行なったのち、洗浄排水
弁20及び空気洗浄弁21を閉、原水流入弁18を開と
して濾過操作を再開することにより、清澄な処理水を容
易に得ることができる。
(31p Resuming the filtration process After performing backwashing in this way for a certain period of time, the washing drain valve 20 and the air washing valve 21 are closed, the raw water inflow valve 18 is opened, and the filtration operation is resumed, thereby producing clear treated water. can be obtained easily.

なお、本考案においては前記逆U字配管の代わりに第4
図のような構造のものを適用することもできる。
In addition, in the present invention, instead of the above-mentioned inverted U-shaped piping, a fourth piping is used.
A structure as shown in the figure can also be applied.

図中、31は箱状体である。以上述べたように本考案に
よれば、次のような利点が得られる。
In the figure, 31 is a box-shaped body. As described above, according to the present invention, the following advantages can be obtained.

■ 従来の空気洗浄を行なう重力式濾過槽体においては
中間排水を行なうさい、濾過水流出管または濾過水流出
管兼逆洗水管に弁を配設し、その都度開閉操作を行なう
必要があったが、前記濾過水流出弁、濾過水流出兼逆洗
用の弁を配設することなく中間排水が行なえる利点があ
る。
■ In conventional gravity-type filtration tanks that perform air cleaning, when performing intermediate drainage, it was necessary to install a valve in the filtrate outflow pipe or the filtrate outflow pipe and backwash water pipe, and open and close it each time. However, there is an advantage that intermediate drainage can be performed without providing the filtrate outflow valve and the filtrate outflow/backwash valve.

また、濾過水流出管兼逆洗水管の口径は逆洗水量の流速
によって決定され、このため濾過水流出兼逆洗用の弁の
口径が大きくなり、前記の弁を中間排水のためにのみ自
動弁にすることは不経済であるが、本考案の装置ではこ
のような弁は不要となるので設備費が節減できる。
In addition, the diameter of the filtrate outflow pipe and backwash water pipe is determined by the flow rate of the amount of backwash water, so the diameter of the valve for filtrate outflow and backwashing becomes large, and the above valve is automatically used only for intermediate drainage. Although it is uneconomical to use a valve, the device of the present invention does not require such a valve, so equipment costs can be reduced.

■ 機械的制御または特別な操作などを必要とせず空気
洗浄時に水位を所定の位置まで降下させて炉材の流出損
失を防止することができ、その構成も簡易で安価であり
、濾過持続時間も長くし濾過操作に支障をきたすことな
く安定した運転が可能で、保守保安も著しく簡便である
■ It is possible to prevent the loss of furnace material by lowering the water level to a predetermined position during air cleaning without requiring mechanical control or special operations, and its configuration is simple and inexpensive, and the filtration duration is short. The length allows stable operation without hindrance to filtration operations, and maintenance and safety are extremely simple.

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

図面は本考案の実施例を示腰第1図は正面断面図、第2
図及び第3図は操作手順の説明図であり、第4図はサイ
フオン形成管の別の実施例を示す部分正面断面図である
The drawings show an embodiment of the present invention. Figure 1 is a front sectional view,
3 and 3 are explanatory diagrams of the operating procedure, and FIG. 4 is a partial front sectional view showing another embodiment of the siphon forming tube.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 空気洗浄機構を備えた重力式濾過槽において、該槽内を
仕切壁にて濾過室と排水渠とに区画し、前記濾過室に炉
材層とその下方部に集水室を備え、前記炉材層の上方部
に逆洗排水樋を配設すると共に該逆洗排水樋と炉材層と
の間に中間排水管を設け、前記逆洗排水樋を前記仕切壁
を介して前記排水渠に開口連通させ、さらに前記集水室
と濾過水流出渠とをサイフオンブレーカ−を付設したサ
イフオン形成管にて連通してなる重力式濾過装置。
In a gravity type filtration tank equipped with an air cleaning mechanism, the inside of the tank is divided into a filtration chamber and a drain by a partition wall, the filtration chamber is provided with a furnace material layer and a water collection chamber below it, and the furnace A backwash drain gutter is provided above the material layer, and an intermediate drain pipe is provided between the backwash drain gutter and the furnace material layer, and the backwash drain gutter is connected to the drain through the partition wall. A gravity type filtration device in which the water collection chamber and the filtrate outflow conduit are communicated through a siphon forming pipe provided with a siphon breaker.
JP11670681U 1981-08-07 1981-08-07 gravity filtration device Expired JPS6022964Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11670681U JPS6022964Y2 (en) 1981-08-07 1981-08-07 gravity filtration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11670681U JPS6022964Y2 (en) 1981-08-07 1981-08-07 gravity filtration device

Publications (2)

Publication Number Publication Date
JPS5823608U JPS5823608U (en) 1983-02-15
JPS6022964Y2 true JPS6022964Y2 (en) 1985-07-09

Family

ID=29910915

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11670681U Expired JPS6022964Y2 (en) 1981-08-07 1981-08-07 gravity filtration device

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JP2965295B2 (en) * 1986-10-01 1999-10-18 堯之 久原 Operation control method of thermal storage tank with multiple water tanks

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JPS5823608U (en) 1983-02-15

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