JPS6130809B2 - - Google Patents
Info
- Publication number
- JPS6130809B2 JPS6130809B2 JP57031512A JP3151282A JPS6130809B2 JP S6130809 B2 JPS6130809 B2 JP S6130809B2 JP 57031512 A JP57031512 A JP 57031512A JP 3151282 A JP3151282 A JP 3151282A JP S6130809 B2 JPS6130809 B2 JP S6130809B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- water
- backwash
- chamber
- filtration
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 89
- 238000011001 backwashing Methods 0.000 claims description 32
- 238000001914 filtration Methods 0.000 claims description 32
- 230000001105 regulatory effect Effects 0.000 claims description 17
- 238000007654 immersion Methods 0.000 claims description 2
- 239000000463 material Substances 0.000 description 5
- 230000033228 biological regulation Effects 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 238000005406 washing Methods 0.000 description 3
- 230000000630 rising effect Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Description
【発明の詳細な説明】
本発明は適正な逆洗速度で逆洗を行なうことの
できるいわゆる逆洗水自己保有形の過装置に関
するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a so-called backwash water self-containing type filtration device capable of backwashing at an appropriate backwash rate.
従来この種の装置として第1図に示すものがあ
つた。図において1はいわゆる逆洗水自己保有形
過装置(以下単に「過装置」という)、2は
過タンク、3は過タンク2の上部に設けられ
た逆洗タンク、2aは原水入口、3aは水出口
である。又4は過タンク2内に設けられた浄化
室であり、該浄化室4は上方より原水室5、過
層6及び水室7に順次画成されており、更に5
aは原水室5の上部長手方向の内側端に傾斜して
設けられたトラフである。8は逆洗タンク3と
水室7を連通する為の連通管、9は過タンク2
に取付けられた逆洗排水弁、10は排水溝であ
る。この様な過装置1では原水は原水入口2a
から過タンク2内に導かれた後、浄化室4を上
方から通過する間に過層6で浄化され、水は
水室7から連通管8を上昇して逆洗タンク3内
に導かれる。そして一定の水位に達すると、水
出口3aから排出される。従つて逆洗タンク3内
には常に一定水位の水が保有された状態となつ
ており、この保有水が逆洗時には逆洗水として
利用される。即ち逆洗に当つて逆洗排水弁9を開
けると、保有水(以下「逆洗水」と称する)R
は連通管8を下降して水室7に流入し、更に
過層6を上昇し(即ち逆流)することにより過
層6の洗浄を行なう。この洗浄水は上方の原水室
5から傾斜トラフ5aに溢れ出た後、洗浄水出口
5a′から流下し、更に逆洗排水弁9から外部の排
水槽10に排出される。 A conventional device of this type is shown in FIG. In the figure, 1 is a so-called backwash water self-contained filtration device (hereinafter simply referred to as "filtration device"), 2 is a filtration tank, 3 is a backwash tank installed at the top of the filtration tank 2, 2a is a raw water inlet, and 3a is a This is the water outlet. Further, 4 is a purification chamber provided in the overtank 2, and the purification chamber 4 is divided into a raw water chamber 5, an overlayer 6, and a water chamber 7 in order from above.
A is a trough provided at an inclined inner end of the upper longitudinal direction of the raw water chamber 5. 8 is a communication pipe for communicating the backwash tank 3 and the water chamber 7, and 9 is the overtank 2.
A backwash drain valve is attached to 10, and 10 is a drain. In such a filtration device 1, raw water is supplied to the raw water inlet 2a.
After being led into the overlayer tank 2, the water is purified in the overlayer 6 while passing through the purification chamber 4 from above, and then ascends from the water chamber 7 through the communication pipe 8 and is led into the backwash tank 3. When the water level reaches a certain level, the water is discharged from the water outlet 3a. Therefore, water at a constant level is always held in the backwash tank 3, and this held water is used as backwash water during backwashing. That is, when the backwash drain valve 9 is opened during backwashing, retained water (hereinafter referred to as "backwash water") R
The water flows down the communication pipe 8, flows into the water chamber 7, and further rises (that is, flows backward) through the overlayer 6, thereby cleaning the overlayer 6. This wash water overflows from the upper raw water chamber 5 into the inclined trough 5a, flows down from the wash water outlet 5a', and is further discharged from the backwash drain valve 9 to the external drain tank 10.
従来の過装置は上記の如く該装置1によつて
浄化された水を逆洗水として使用すると共に、
逆洗水を過タンク2の上部に保有して、保有時
の水頭を利用して過タンク2内の過層6の洗
浄を行なうようにしているので、別途逆洗装置を
要せず経済的である。しかし下記の如き大きな欠
点もあつた。逆洗は単に水頭による逆洗水を利
用するものであるから、水位が変化すれば逆洗水
が過層6を通過する速度(以下これを「逆洗速
度」という)が変わつてしまう。特に逆洗初期に
は水位が高いので水頭が大きく、その為逆洗速度
が適正逆洗速度よりも大き過ぎて過層6の材
が浄化室4から流出する。反対に逆洗終期には水
位が低いので水頭が小さく、その為逆洗速度が適
正逆洗速度よりも小さ過ぎて過層6の浄化を十
分に行なえない。過層6の浄化を行なつた逆
洗水の通路となる傾斜トラフ5aは原水室5の上
部内側に設けているので、該トラフ5aの平面積
に対応する部分の材は有効な浄化が行なわれ
ず、その分逆洗効率が低下する。 The conventional filtration device uses the water purified by the device 1 as backwash water as described above, and
Since the backwash water is stored in the upper part of the overtank 2 and the water head at the time of holding is used to wash the overlayer 6 in the overtank 2, a separate backwashing device is not required and it is economical. It is. However, there were also major drawbacks as described below. Since backwashing simply utilizes backwash water due to water head, if the water level changes, the speed at which backwash water passes through the overlayer 6 (hereinafter referred to as "backwash speed") will change. Particularly in the initial stage of backwashing, the water level is high, so the water head is large, and therefore the backwashing speed is too high than the appropriate backwashing speed, and the material of the overlayer 6 flows out of the purification chamber 4. On the other hand, at the end of backwashing, the water level is low, so the water head is small, and therefore the backwashing speed is too low than the appropriate backwashing speed, and the overlayer 6 cannot be sufficiently purified. Since the inclined trough 5a, which serves as a passage for backwash water that has purified the overlayer 6, is provided inside the upper part of the raw water chamber 5, the material in the area corresponding to the planar area of the trough 5a is effectively purified. Therefore, the backwashing efficiency decreases accordingly.
本発明はこうした事情に着目してなされたもの
でその目的とする所は、逆洗速度を適正に制御す
ることのできる逆洗性能の優れた過装置を提供
しようとするにある。 The present invention has been made in view of these circumstances, and its purpose is to provide a filtration device with excellent backwash performance that can appropriately control the backwash speed.
しかしてこの様な目的を達成し得た本発明の
過装置とは、上方より原水室、過層及び水室
に順次画成されてなる過タンクの上部に逆洗タ
ンクを設けると共に該タンクと前記水室を連通
し、且つ前記原水室の外側近傍には原水室と外部
を連通する逆洗排水弁を設けて、該排水弁の開閉
により前記逆洗タンク内に逆洗水を前記過タン
ク内に導入し通過させることによつて前記過層
の逆洗を行なうようにしてなる過装置におい
て、前記逆洗排水弁出口側を、濾過タンクの外部
に設けた水封調圧タンクの調圧空気室に接続する
一方、前記逆洗タンク内部には、外部の圧縮空気
源に連結され且つ前記逆洗タンクの底部で開口す
る圧縮空気配管を設けて該圧縮空気配管と前記水
封調圧タンクの調圧空気室とを連通させて構成し
た点に要旨を有するものである。 However, the filtration device of the present invention that has achieved these objectives is a filtration tank that is formed from above into a raw water chamber, an overlayer, and a water chamber in order, and a backwash tank is provided on the upper part of the filtration tank. A backwash drain valve is provided near the outside of the raw water chamber and communicates the raw water chamber with the outside, and by opening and closing the drain valve, backwash water is transferred into the backwash tank into the overtank. In a filtration device that backwashes the superlayer by introducing water into the filtration tank and allowing it to pass through, the backwash drain valve outlet side is provided outside the filtration tank for pressure regulation of a water-sealed pressure regulation tank. While connected to the air chamber, a compressed air pipe connected to an external compressed air source and opened at the bottom of the backwash tank is provided inside the backwash tank, and the compressed air pipe and the water seal pressure regulation tank are connected to each other. The gist lies in that the pressure regulating air chamber is configured to communicate with the pressure regulating air chamber.
以下本発明の一実施例を図面に基づいて説明す
る。第2図は本発明に係る過装置の概略説明図
であり、この図において11は過装置、12は
過タンク、13は過タンク12の上部に設け
られた逆洗タンク、12aは原水入口、13aは
水出口である。又過タンク12は上方より原
水室15、過層16及び水室17に順次画成
されている。18は逆洗タンク13と水室17
を連通する為の連通管である。又原水室15の上
部には外部と連通する集水管21が配設され、且
つ集水管21にはストレーナ22が適当な間隔を
おいて複数取付けられている。更に集水管21の
うち、原水室15の外側近傍には逆洗排水弁19
を取付けると共に該排水弁19の出口側管23は
外部に設けた調圧タンク24の側面に連結してい
る。調圧タンク24は排水槽25内で水封されて
いる。又逆洗タンク13の内部には、空気圧縮機
26に連結され且つ逆洗タンク13の底部で開口
する圧縮空気配管27を設けている。更に該配管
27と調圧タンク24の上面は連通管28によつ
て連通されている。又29は排水槽25から溢れ
出た逆洗水を流下し易くする為のガイド板、20
は排水溝である。尚調圧タンク24の調圧空気室
29及び水封室30は圧縮空気配管27の逆洗タ
ンク13への最大浸漬深さ、即ち逆洗タンク13
の水面が最も高い時の深さを有する様に構成され
ている。 An embodiment of the present invention will be described below based on the drawings. FIG. 2 is a schematic explanatory diagram of a filtration device according to the present invention. In this figure, 11 is a filtration device, 12 is a filtration tank, 13 is a backwash tank provided at the upper part of the filtration tank 12, 12a is a raw water inlet, 13a is a water outlet. Further, the overtank 12 is defined in order from above into a raw water chamber 15, an overlayer 16, and a water chamber 17. 18 is the backwash tank 13 and water chamber 17
It is a communication pipe for communicating. Further, a water collection pipe 21 communicating with the outside is disposed in the upper part of the raw water chamber 15, and a plurality of strainers 22 are attached to the water collection pipe 21 at appropriate intervals. Furthermore, in the water collection pipe 21, a backwash drain valve 19 is installed near the outside of the raw water chamber 15.
At the same time, the outlet pipe 23 of the drain valve 19 is connected to the side surface of a pressure regulating tank 24 provided outside. The pressure regulating tank 24 is sealed with water inside a drainage tank 25. Further, inside the backwash tank 13, a compressed air pipe 27 is provided which is connected to an air compressor 26 and opens at the bottom of the backwash tank 13. Further, the pipe 27 and the upper surface of the pressure regulating tank 24 are communicated with each other by a communication pipe 28. Further, 29 is a guide plate for making it easier for backwash water overflowing from the drain tank 25 to flow down, 20
is a drainage ditch. The pressure regulating air chamber 29 and water seal chamber 30 of the pressure regulating tank 24 are set at the maximum immersion depth of the compressed air pipe 27 into the backwash tank 13, that is, the backwash tank 13.
The depth is the same as when the water surface is at its highest.
この様に構成された過装置11における過
操作は第1図の従来例と同様であり、以下特徴あ
る逆洗操作について説明する。逆洗に当つては空
気圧縮機26を作動し、弁30,31は開けて弁
32は閉じてく。次いで逆洗排水弁19を開ける
と、逆洗水Rは連通管18を下降して水室17
に流入し始め、逆洗が開始されるが、開始後の逆
洗速度は下記する如く本発明の特有の構成及び作
用により適正に制御される。即ち逆洗タンク18
内における圧縮空気配管27の開口面を基準位L
として、この準位から調圧タンク24の入口24
aの準位L1までをHo、逆洗タンク13内におけ
る逆洗水Rの任意の準位L2までをhとすると、
調圧タンク24内は水頭hに相当する背圧を受け
るので、調圧タンク24の入口24aでの水頭は
全水頭(Ho+h)−背圧h=Ho(一定)とな
る。即ち逆洗タンク13内の水位が基準位Lに降
下するまでは調圧タンク24内には常に一定の水
頭が作用するので排水槽25から排水溝20に溢
流する逆洗水量も一定となる。かくして逆洗タン
ク13内の水位の変動にかかわらず逆洗速度は一
定となる。さて逆洗は、逆洗水Rが連通管18を
下降して水室17に流入した後、過層16を
上昇して該過層16を洗浄することによつて行
なうが、このときの逆洗水の上昇速度は上記の如
く逆洗初期から逆洗終期にわたつて一定である。
従つて従来の様に逆洗初期における材の流出現
象は起こらず、又逆洗終期における逆洗性能の著
しい低下ということも起こらない。過層16の
洗浄を行なつた逆洗水はストレーナ22で微細
材が分離された後、集水管21を経て原水室15
の外部へ導かれる。即ち過層16の浄化を行な
つた逆洗水の通路は、原水室15の上部に設けた
集水管21で達成したので、従来の様な傾斜トラ
フの採用下で生じていた過有効面積の減少に伴
う設備効率の低下を防止することができる。上記
装置により適宜逆洗を実施することによつて長期
間安定した濾過成積を得ることができた。 The over-washing operation in the overwashing device 11 constructed in this way is similar to the conventional example shown in FIG. 1, and the characteristic backwashing operation will be explained below. For backwashing, the air compressor 26 is operated, valves 30 and 31 are opened, and valve 32 is closed. Next, when the backwash drain valve 19 is opened, the backwash water R descends through the communication pipe 18 and enters the water chamber 17.
The backwashing speed after the start of backwashing is properly controlled by the unique structure and operation of the present invention as described below. That is, the backwash tank 18
The opening surface of the compressed air pipe 27 inside the reference position L
From this level, the inlet 24 of the pressure regulating tank 24
Let Ho be up to the level L 1 of a, and h be the arbitrary level L 2 of the backwash water R in the backwash tank 13.
Since the inside of the pressure regulating tank 24 receives a back pressure corresponding to the water head h, the water head at the inlet 24a of the pressure regulating tank 24 is total water head (Ho+h) - back pressure h=Ho (constant). That is, until the water level in the backwash tank 13 drops to the reference level L, a constant water head always acts in the pressure regulating tank 24, so the amount of backwash water overflowing from the drain tank 25 to the drain groove 20 is also constant. . In this way, the backwash speed remains constant regardless of fluctuations in the water level in the backwash tank 13. Now, backwashing is performed by backwashing water R descending down the communication pipe 18 and flowing into the water chamber 17, and then rising up the overlayer 16 and washing the overlayer 16. As mentioned above, the rising speed of the washing water is constant from the beginning of backwashing to the end of backwashing.
Therefore, the outflow phenomenon of material at the beginning of backwashing does not occur as in the conventional case, nor does a significant decrease in backwashing performance at the end of backwashing occur. The backwash water used to wash the overlayer 16 is separated into fine materials by the strainer 22, and then passes through the water collection pipe 21 to the raw water chamber 15.
led to the outside of In other words, the passage of the backwash water that purified the overlayer 16 was achieved through the water collection pipe 21 installed at the top of the raw water chamber 15, which saved the over-effective area that would have occurred when using a conventional inclined trough. It is possible to prevent a decrease in equipment efficiency due to the decrease. By appropriately performing backwashing using the above device, a stable filtration product could be obtained for a long period of time.
本発明の過装置は概略以上の記く構成される
が、要は逆洗排水弁の出口側に逆洗タンクと連通
する水封調圧タンクを設けて該調圧タンクに一種
の流量制御弁的機能を営ましめるように成したの
で、逆洗速度を適正に制御できる様になつた。従
つて逆洗初期の材流出や逆洗終期の逆洗速度の
低下を防止できる様になり、逆洗性能の優れた
過装置とすることができた。 The filtering device of the present invention has a configuration as described above, but the key point is that a water-sealed pressure regulating tank is provided on the outlet side of the backwashing drain valve and communicates with the backwashing tank, and the pressure regulating tank is provided with a type of flow control valve. The backwashing speed can now be controlled appropriately. Therefore, it became possible to prevent the material from flowing out at the beginning of backwashing and the reduction in backwashing speed at the end of backwashing, making it possible to provide a filtration device with excellent backwashing performance.
第1図は従来の過装置の概略説明図、第2図
は本発明に係る過装置の概略説明図を夫々示
す。
11…過装置、12…過タンク、13…逆
洗タンク、15…原水室、16…過層、17…
水室、18…連通管、19…逆洗排水弁、21
…集水管、24…調圧タンク、26…空気圧縮
機、27…圧縮空気配管、28…連通管。
FIG. 1 is a schematic illustration of a conventional filtering device, and FIG. 2 is a schematic illustration of a filtering device according to the present invention. 11... filtration device, 12... filtration tank, 13... backwash tank, 15... raw water chamber, 16... superlayer, 17...
Water chamber, 18...Communication pipe, 19...Backwash drain valve, 21
... Water collection pipe, 24 ... Pressure regulation tank, 26 ... Air compressor, 27 ... Compressed air piping, 28 ... Communication pipe.
Claims (1)
成されてなる濾過タンクの上部に逆洗タンクを設
けると共に該タンクと前記濾水室を連通し、且つ
前記原水室の外側近傍には原水室と外部を連通す
る逆洗排水弁を設けて、該排水弁の開閉により前
記逆洗タンク内の逆洗水を前記濾過タンク内に導
入し通過させることによつて前記濾過層の逆洗を
行なうようにしてなる濾過装置において、前記逆
洗排水弁出口側を、濾過タンクの外部に設けた水
封調圧タンクの調圧空気室に接続する一方、前記
逆洗タンク内部には、外部の圧縮空気源に連結さ
れ且つ前記逆洗タンクの底部で開口する圧縮空気
配管を設けて該圧縮空気配管と前記水封調圧タン
クの調圧空気室とを連通させ、前記水封調圧タン
クにおける調圧空気室及び該空気室の出側に設け
られる水封室は前記圧縮空気配管の逆洗タンクへ
の最大浸漬深さを越える高さを夫々有する様に構
成してなることを特徴とする過装置。1. A backwash tank is provided at the top of a filtration tank which is defined from above into a raw water chamber, a filtration layer, and a filtration chamber, and the tank and the filtration chamber are communicated, and near the outside of the raw water chamber. A backwash drain valve communicating with the raw water chamber and the outside is provided, and the backwash water in the backwash tank is introduced into and passed through the filtration tank by opening and closing the drain valve, thereby backwashing the filtration layer. In a filtration device configured to perform A compressed air piping connected to a compressed air source and opening at the bottom of the backwash tank is provided to communicate the compressed air piping with the pressure regulating air chamber of the water seal pressure regulating tank, and the water seal pressure regulating tank The pressure regulating air chamber and the water seal chamber provided on the outlet side of the air chamber are each configured to have a height exceeding the maximum immersion depth of the compressed air piping into the backwash tank. over device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57031512A JPS58150405A (en) | 1982-02-27 | 1982-02-27 | filtration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57031512A JPS58150405A (en) | 1982-02-27 | 1982-02-27 | filtration device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58150405A JPS58150405A (en) | 1983-09-07 |
| JPS6130809B2 true JPS6130809B2 (en) | 1986-07-16 |
Family
ID=12333258
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57031512A Granted JPS58150405A (en) | 1982-02-27 | 1982-02-27 | filtration device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58150405A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104383728B (en) * | 2014-11-18 | 2016-08-24 | 中国建筑设计院有限公司 | Pressure type roof rainwater treatment, storage and reuse integrated device |
-
1982
- 1982-02-27 JP JP57031512A patent/JPS58150405A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58150405A (en) | 1983-09-07 |
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