JPS5855801B2 - Sedimentation tank with filter - Google Patents
Sedimentation tank with filterInfo
- Publication number
- JPS5855801B2 JPS5855801B2 JP52131865A JP13186577A JPS5855801B2 JP S5855801 B2 JPS5855801 B2 JP S5855801B2 JP 52131865 A JP52131865 A JP 52131865A JP 13186577 A JP13186577 A JP 13186577A JP S5855801 B2 JPS5855801 B2 JP S5855801B2
- Authority
- JP
- Japan
- Prior art keywords
- filter
- valve
- sedimentation tank
- detector
- pump
- 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
- 238000004062 sedimentation Methods 0.000 title claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 25
- 238000001914 filtration Methods 0.000 claims description 13
- 238000011001 backwashing Methods 0.000 claims description 5
- 238000001514 detection method Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 description 7
- 239000010802 sludge Substances 0.000 description 5
- 239000002351 wastewater Substances 0.000 description 5
- 238000005273 aeration Methods 0.000 description 4
- 238000006386 neutralization reaction Methods 0.000 description 4
- 238000005554 pickling Methods 0.000 description 4
- 238000005192 partition Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Description
【発明の詳細な説明】
本発明は活性汚泥法や回転曝気法や酸洗い廃水の中和処
理等によって処理した汚水を沈澱処理するのに使用する
沈澱槽に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a settling tank used for settling wastewater treated by an activated sludge method, a rotary aeration method, a neutralization treatment of pickling wastewater, or the like.
従来、活性汚泥法や回転曝気法や酸洗い廃水の中和処理
等によって処理した汚水を沈澱処理するのに使用する沈
澱槽においては微小フロックがキャリーオーバーし、処
理水質を悪化させるケースが多かった。Conventionally, in settling tanks used to settle sewage treated by the activated sludge method, rotary aeration method, or neutralization of pickling wastewater, there were many cases in which micro flocs carried over and deteriorated the quality of the treated water. .
本発明の目的は流入口と流出越流基を有する沈澱室と、
前記流出越流基の出口側と連通ずるとともにフィルタを
有する排水口と一定条件下において処理水を流出する補
助排水口と一定高さの水位を検出するレベル計と該レベ
ル計の検出信号により作動する前記フィルタの逆洗機構
とを有する濾過室とを備え、微小フロックも除去するご
とくした沈澱槽を提供せんとすることである。The object of the present invention is to provide a settling chamber having an inlet and an outlet overflow base;
A drain port that communicates with the outlet side of the outflow overflow base and has a filter, an auxiliary drain port that drains treated water under certain conditions, a level meter that detects a water level at a certain height, and is activated by the detection signal of the level meter. It is an object of the present invention to provide a settling tank which is equipped with a filtration chamber having a backwashing mechanism for the filter, and is capable of removing even minute flocs.
以下、図に示す一実施例に基づいて本発明を説明する。The present invention will be described below based on an embodiment shown in the drawings.
1は沈澱室であり、2は流入口であり流入管3が結合さ
れている。1 is a precipitation chamber, 2 is an inlet, and an inflow pipe 3 is connected thereto.
4は流入室であり、5はその流入越流基である。4 is an inflow chamber, and 5 is its inflow overflow base.
6は流出越流基であり、7は流出室である。6 is an outflow overflow base, and 7 is an outflow chamber.
8及び9は隔壁であり、流入越流基5と流出越流基6と
の間において水面近くの短絡水流を遮断するごとく設げ
られている。Reference numerals 8 and 9 indicate partition walls, which are provided between the inflow overflow base 5 and the outflow overflow base 6 so as to block short-circuit water flow near the water surface.
10は濾過室であり、連通管11が流出室7から濾過室
10へ開口して連通している。10 is a filtration chamber, and a communication pipe 11 opens and communicates with the filtration chamber 10 from the outflow chamber 7.
12はフィルタであり、排水管13の内端部に取着され
排水口となっている。Reference numeral 12 denotes a filter, which is attached to the inner end of the drain pipe 13 and serves as a drain port.
14はレベル計であり、一定高さの水位を検出するごと
く設けられており、フィルタ120目詰まりを検出する
検出器となってちる。Reference numeral 14 denotes a level meter, which is provided to detect a water level at a certain height, and serves as a detector for detecting clogging of the filter 120.
15は補助排水口であり、補助排水管16に連結されて
いる。15 is an auxiliary drain port, which is connected to an auxiliary drain pipe 16.
補助排水口15はレベル計14で検出する一定高さの水
位よりも若干上方の位置に設けられており、この位置は
通常の水位よりも高い位置にある一定高さの位置となっ
ている。The auxiliary drain port 15 is provided at a position slightly above the water level at a certain height detected by the level meter 14, and this position is at a certain height higher than the normal water level.
斜動排水管16の他端は、活性汚泥法や回転曝気θや酸
洗い廃水の中和処理等によって処理する以イの原水槽へ
連通している。The other end of the diagonal drainage pipe 16 communicates with a raw water tank which is treated by the activated sludge method, rotary aeration θ, neutralization of pickling wastewater, or the like.
排水管13はバルブ1γに連通しており、バルブ17は
排水管18を通してポンプ井19へ開口している。Drain pipe 13 communicates with valve 1γ, and valve 17 opens to pump well 19 through drain pipe 18.
20はポンプ井19内に設けられたポンプであり、ポン
プ20は連通管21,22、バルブ23、連通管24に
よって排水管13に連通している。20 is a pump provided in the pump well 19, and the pump 20 communicates with the drain pipe 13 through communication pipes 21, 22, a valve 23, and a communication pipe 24.
また、ポンプ20は連通管21,25、バルブ26を通
して、放流管27に連通しており、放流管27は適宜放
流域へ開口している。Further, the pump 20 communicates with a discharge pipe 27 through communication pipes 21, 25 and a valve 26, and the discharge pipe 27 opens into the discharge area as appropriate.
28,29は汚泥耕出管であり、30はバルブである。28 and 29 are sludge cultivation pipes, and 30 is a valve.
ポンプ20、パル7”17,23,26等は逆洗機構を
構成してイル。The pump 20, pallets 7'' 17, 23, 26, etc. constitute a backwashing mechanism.
また、フィルタ120目詰まりを検出する検出器として
は排水口の流速を検出して目詰まりを検出するごと(す
ることもできる。Further, as a detector for detecting clogging of the filter 120, it is also possible to detect clogging by detecting the flow velocity of the drain port.
しかして、活性汚泥法や回転曝気法や酸洗い廃水の中和
処理等によって処理されてフロックを含んだ処理水が流
入管3内を流れて流入口2より流入室4へ流入し、流入
越流堰5を越流して静かに沈澱室1へ流入し、大きなフ
ロックが沈澱する。The treated water containing flocs, which has been treated by the activated sludge method, rotary aeration method, neutralization of pickling wastewater, etc., flows through the inflow pipe 3, flows into the inflow chamber 4 from the inflow port 2, and flows over the inflow. The water overflows the flow weir 5 and flows quietly into the settling chamber 1, where large flocs are settled.
フロックが沈澱した処理水の上澄液は流出越流堰6を越
流して流出室7へ流出し、連通管11によって濾過室1
0へ流入する。The supernatant liquid of the treated water in which the flocs have precipitated overflows the outflow overflow weir 6 and flows into the outflow chamber 7, and is transferred to the filtration chamber 1 through the communication pipe 11.
Flows into 0.
沈澱室1においては隔壁8,9があるためフロックを含
んだ水が流入越流堰5から流出越流堰へ直接短絡して流
れるのが防止されている。In the settling chamber 1, the partition walls 8 and 9 prevent water containing flocs from directly short-circuiting and flowing from the inlet overflow weir 5 to the outflow overflow weir.
濾過室10へ流入した処理水ニハ微小フロックが含まれ
ており、この微小フロックはフィルタ12によって濾過
され、微小フロックが除去された処理水は排水管13、
バルブ17、排水管18を通ってポンプ井19へ流入す
る。The treated water that has flowed into the filtration chamber 10 contains minute flocs, and these minute flocs are filtered by the filter 12, and the treated water from which the minute flocs have been removed is drained into the drain pipe 13,
It flows into the pump well 19 through the valve 17 and the drain pipe 18.
通常バルブ23は閉となっており、バルブ26は開とな
っているので、ポンプ井19の微小フロックを除去され
た処理水はポンプ20によって連通管21,25、バル
ブ26、放流管27を通して適宜放流される。Normally, the valve 23 is closed and the valve 26 is open, so the treated water from the pump well 19 from which minute flocs have been removed is passed through the communication pipes 21, 25, the valve 26, and the discharge pipe 27 by the pump 20 as appropriate. It is released into the river.
フィルタ12が目詰まりを起こすと、濾過室10の処理
水は流出が阻止されるため、濾過室10の水面が上昇し
一定高さの水位に達するとレベル計14が検出し、その
検出信号により、バルブ23が開となるとともにバルブ
17及び26が閉となる。When the filter 12 becomes clogged, the treated water in the filtration chamber 10 is blocked from flowing out, so when the water level in the filtration chamber 10 rises and reaches a certain level, the level meter 14 detects it, and the detection signal , valve 23 is opened and valves 17 and 26 are closed.
このためポンプ20かも送り出される処理水は連通管2
1,22、バルブ23、連通管24を通って排水管13
を逆流しフィルタ12から濾過室10へ流入する。Therefore, the treated water sent out by the pump 20 is also sent to the communication pipe 2.
1, 22, the valve 23, and the drain pipe 13 through the communication pipe 24.
flows back into the filtration chamber 10 from the filter 12.
このためフィルタ12は逆□流によって洗浄(逆洗)さ
れる。For this reason, the filter 12 is washed (backwashed) by the reverse □ flow.
濾過室10内の処理水は補助排水管16を通って原水槽
へ返送される。The treated water in the filtration chamber 10 is returned to the raw water tank through the auxiliary drain pipe 16.
レベル計14の信号から一定時間後タイマ等により、バ
ルブ17゜23.26が切り換わり、バルブ17,26
が開となり、バルブ23が閉となり、通常の通路を通っ
て処理水は放流される。After a certain period of time from the signal from the level meter 14, the valves 17, 26 are switched by a timer or the like.
is opened, the valve 23 is closed, and the treated water is discharged through the normal passage.
以上のごとく本発明は微小フロックがフィルタによって
濾過されるためBOD等の除去率が向上し、微小フロッ
クを沈澱させるだけの長い滞留時間が必要でないから装
置が小型となり、沈澱室と濾過室を隔離したため大きな
フロックは沈澱し濾過室へは微小なフロックのみが流入
するためフィルタの目詰まりが少なくなり、フィルタの
目詰まりが起ると逆洗されて目詰まりが除去され、良好
な処理が行なわれる。As described above, in the present invention, since micro flocs are filtered by the filter, the removal rate of BOD etc. is improved, and since the long residence time required to precipitate the micro flocs is not required, the device becomes compact and the precipitation chamber and filtration chamber are separated. As a result, large flocs are precipitated and only minute flocs flow into the filtration chamber, resulting in less clogging of the filter, and when the filter is clogged, it is backwashed to remove the clog and ensure good treatment. .
図はいずれも本発明の一実施例を示す説明的断面図であ
り、第1図は通常の場合、第2図は逆洗時の場合を示す
。
1・・・・・・沈澱室、2・・・・・・流入口、6・・
・・・・流出越流堰、10・・・・・・濾過室、12・
・・・・・フィルタ(排水口)、13・・・・・・排水
管、14・・・・・・レベル計、15・・・・・・補助
排水口、16・・・・・・補助排水管、17,23゜2
5・・・・・・バルブ、19・・・・・・ポンプ井、2
0・・・・・・ポンプ。The figures are all explanatory cross-sectional views showing one embodiment of the present invention, with FIG. 1 showing the normal case and FIG. 2 showing the case during backwashing. 1...Sedimentation chamber, 2...Inlet, 6...
... Outflow overflow weir, 10 ... Filtration chamber, 12.
... Filter (drain port), 13 ... Drain pipe, 14 ... Level meter, 15 ... Auxiliary drain port, 16 ... Auxiliary Drain pipe, 17,23゜2
5... Valve, 19... Pump well, 2
0...Pump.
Claims (1)
流基の出口側と連通ずるとともにフィルタを有する排水
口と一定条件下において処理水を流出する補助排水口と
前記フィルタの目詰まりを検出する検出器と該検出器の
検出信号により作動する前記フィルタの逆洗機構とを有
する濾過室とを備えたフィルタ付沈澱槽。 2、特許請求の範囲1において、検出器として一定高さ
の水位を検出するレベル計としたフィルタ付沈澱槽。 3 特許請求の範囲1において、検出器として排水口の
流速を検出してフィルタの目詰まりを検出するごとくし
たフィルタ付沈澱槽。 4 %許請求の範囲1又は2又は3において、補助排水
口を通常の水位よりも高い位置にある一定高さに設けた
フィルタ付沈澱槽。 5 特許請求の範囲1又は2又は3において、補助排水
口にバルブを設け、逆洗機構が作動中バルブが開となる
ごとくしたフィルタ付沈澱槽。 6 特許請求の範囲1又は2又は3又は4又は5におい
て、逆洗機構をフィルタから排水管をバルブ17を介し
てポンプ井に連通し、ポンプ井に設けたポンプを連通管
によってバルブ23を介して前記排水管に連通するとと
もに前記ポンプを連通管によりバルブ26を介して放流
域に開口し、これらのバルブを検出信号によって制4す
るごとくしたフィルタ付沈澱槽。[Scope of Claims] 1. A settling chamber having an inlet and an outflow overflow base, a drainage port communicating with the outlet side of the outflow overflow base and having a filter, and an auxiliary drainage port through which treated water flows out under certain conditions. and a filtration chamber having a detector for detecting clogging of the filter, and a backwashing mechanism for the filter that is activated by a detection signal from the detector. 2. The sedimentation tank with a filter according to claim 1, which uses a level meter as a detector to detect a water level at a certain height. 3. The sedimentation tank with a filter according to claim 1, which is configured to detect clogging of the filter by detecting the flow velocity of the drain port as a detector. 4. According to claim 1, 2 or 3, the sedimentation tank with a filter is provided with an auxiliary drain at a certain height higher than the normal water level. 5. The sedimentation tank with a filter according to claim 1, 2 or 3, wherein a valve is provided at the auxiliary drain port, and the valve is open while the backwash mechanism is in operation. 6. In claim 1, 2, 3, 4, or 5, the backwashing mechanism is configured such that the filter connects the drain pipe to the pump well via the valve 17, and the pump provided in the pump well is connected to the filter via the valve 23 via the communicating pipe. A sedimentation tank with a filter, which is connected to the drain pipe, and the pump is opened to the discharge area through a valve 26 through a communication pipe, and these valves are controlled by a detection signal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52131865A JPS5855801B2 (en) | 1977-11-02 | 1977-11-02 | Sedimentation tank with filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52131865A JPS5855801B2 (en) | 1977-11-02 | 1977-11-02 | Sedimentation tank with filter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5464769A JPS5464769A (en) | 1979-05-24 |
| JPS5855801B2 true JPS5855801B2 (en) | 1983-12-12 |
Family
ID=15067925
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP52131865A Expired JPS5855801B2 (en) | 1977-11-02 | 1977-11-02 | Sedimentation tank with filter |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5855801B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105688453A (en) * | 2014-11-25 | 2016-06-22 | 无锡市洗选设备厂 | Electrostatic-separation-type sand water precipitation device |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6836026B2 (en) * | 2017-03-31 | 2021-02-24 | 大陽日酸株式会社 | Carburizing device |
-
1977
- 1977-11-02 JP JP52131865A patent/JPS5855801B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105688453A (en) * | 2014-11-25 | 2016-06-22 | 无锡市洗选设备厂 | Electrostatic-separation-type sand water precipitation device |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5464769A (en) | 1979-05-24 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3977970A (en) | Apparatus for and method of filtering solid particles from a particulate-bearing liquid | |
| US3792773A (en) | Apparatus and method for treating waste liquid | |
| CN101475247B (en) | Short process flow water treatment technology with hyperfiltration as core and integrated with multiple water purifying technologies | |
| GB2172216A (en) | Water treatment plant | |
| JP2772612B2 (en) | Water filtration method containing dissolved manganese using permeable membrane | |
| USRE29996E (en) | Upflow filter | |
| JPS5855801B2 (en) | Sedimentation tank with filter | |
| US3642134A (en) | Method and apparatus for tertiary treatment of effluent | |
| JPS6216125B2 (en) | ||
| CN219259776U (en) | Grind effluent disposal system | |
| Hamann et al. | Upflow filtration process | |
| KR102562753B1 (en) | High-speed flocculation and deposition filtration system and water treatment using that | |
| CN215876565U (en) | Rainwater deposits integrative well of filtering | |
| KR200304931Y1 (en) | Small Drinking Water Treatment Equipment | |
| CN209138099U (en) | A kind of efficient concentration filter | |
| US3991781A (en) | Apparatus for and method of automatically cleaning an obstructed valve | |
| CN207412948U (en) | A kind of filtering cloth filtering pool | |
| JP3106859B2 (en) | Settling pond filtration equipment | |
| CN112876004A (en) | Water plant operation system and process method thereof | |
| JPH1147511A (en) | Filtration pond and its operation method | |
| JPH0728886Y2 (en) | Gravity filter | |
| JPS591682Y2 (en) | Sedimentation separator | |
| JPS6333883B2 (en) | ||
| JPH0225456Y2 (en) | ||
| JP3465383B2 (en) | Filtration method of downflow filtration device |