JPH04367793A - Flow adjustment of purification tank - Google Patents

Flow adjustment of purification tank

Info

Publication number
JPH04367793A
JPH04367793A JP16905591A JP16905591A JPH04367793A JP H04367793 A JPH04367793 A JP H04367793A JP 16905591 A JP16905591 A JP 16905591A JP 16905591 A JP16905591 A JP 16905591A JP H04367793 A JPH04367793 A JP H04367793A
Authority
JP
Japan
Prior art keywords
tank
chamber
water
anaerobic filter
aerophobic
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.)
Granted
Application number
JP16905591A
Other languages
Japanese (ja)
Other versions
JP3120814B2 (en
Inventor
Eiichi Nonaka
野中 英市
Masahide Ohara
大屋 雅英
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.)
NISHIHARA NEO KOGYO KK
Original Assignee
NISHIHARA NEO KOGYO 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 NISHIHARA NEO KOGYO KK filed Critical NISHIHARA NEO KOGYO KK
Priority to JP03169055A priority Critical patent/JP3120814B2/en
Publication of JPH04367793A publication Critical patent/JPH04367793A/en
Application granted granted Critical
Publication of JP3120814B2 publication Critical patent/JP3120814B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Treatment Of Biological Wastes In General (AREA)

Abstract

PURPOSE:To prevent a large amount of inflow water from inflicting an impact to a contact aeration tank due to the displacement of a water current by arranging a quantitative discharge pump in a current transfer pipe from the second chamber of an aerophobic filtration bed to the contact aerophobic tank, then isolating a filtration medium from the current transfer pipe and causing a treated water to flow downward from the filtration medium to adjust the flow between the second chamber of the aerophobic filtration bed tank and the contact aeration tank. CONSTITUTION:An aerophobic filtration bed tank or a sedimentation segregation tank, an aeration tank 40, a sedimentation tank 50 and a sterilization tank 60 are arranged sequentially. Then the aerophobic filtration bed chamber or the sedimentation segregation tank is divided into the first chamber 20 and the second chamber 30. Further, a flow adjustment pump 36 for transferring a treated water from the second chamber 30 to the aeration tank 40 is provided in a current transfer pipe 3 from the second chamber 30 to the contact aeration tank 40. The treated water entering the current transfer pipe 34 after passing through a filtration medium 32 in a state of downward current from the second chamber 30, is transferred to the aeration tank 40 by operation of the pump 36. Subsequently, the possible adverse effects of a large amount of inflow water upon the aeration tank in a purification tank is absorbed by the water level variation of the aerophobic filtration bed tank. Thus the purification is free from the turbulence of the treated water flowing out of the aerophobic filtration bed tank by a large amount of inflow water.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、流量調整機能の無い浄
化槽、特に家庭用小形合併浄化槽に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a septic tank without a flow rate adjustment function, and particularly to a small combined septic tank for domestic use.

【0002】0002

【従来の技術】従来の流量調整機能の無い浄化槽にあっ
ては、多量な流入水による悪影響を多分に受けることが
あった。特に、嫌気濾床槽では、次の接触曝気槽への汚
泥の流出などを生じてしまう。すなわち、図3に示すよ
うに、嫌気濾床槽第1室(または沈澱分離槽)20、嫌
気濾床槽第2室30、接触曝気槽40、沈澱槽50、消
毒槽60が直列に配置されることで構成される浄化槽に
おいて、嫌気濾床槽第2室30の移流管34から接触曝
気槽40への流れ(矢印A)が流入水(矢印C)の影響
を受け、流入水(矢印C)が多いと、接触曝気槽40へ
の流れ(矢印A)に嫌気濾床槽第2室の汚泥が入り込ん
でしまうことがある。接触曝気槽40に入り込んだ汚泥
は、散気装置44による曝気処理に影響を及ぼし、消毒
槽60から出る流出水(矢印B)の水質を悪くする。
BACKGROUND OF THE INVENTION Conventional septic tanks without a flow rate adjustment function are often adversely affected by a large amount of inflow water. In particular, in an anaerobic filter bed tank, sludge flows into the next contact aeration tank. That is, as shown in FIG. 3, an anaerobic filter bed tank first chamber (or sedimentation separation tank) 20, an anaerobic filter bed tank second chamber 30, a contact aeration tank 40, a sedimentation tank 50, and a disinfection tank 60 are arranged in series. In a septic tank configured by ), the sludge from the second chamber of the anaerobic filter bed tank may enter the flow to the contact aeration tank 40 (arrow A). The sludge that has entered the contact aeration tank 40 affects the aeration process by the aeration device 44, and deteriorates the quality of the outflow water (arrow B) coming out of the disinfection tank 60.

【0003】従って、従来の浄化槽にあっては、流量調
整のために沈澱分離槽や接触曝気槽の一部を流量調整部
として利用することが考慮されている(例えば、特公昭
58−39836参照)。
[0003] Therefore, in conventional septic tanks, it has been considered to use a part of the sedimentation separation tank or contact aeration tank as a flow rate adjustment section to adjust the flow rate (for example, see Japanese Patent Publication No. 58-39836). ).

【0004】0004

【発明が解決しようとする課題】さらに、流量調整機能
の無い浄化槽の流量調整方法としては、嫌気濾床槽の水
位変動を利用したものがある。
[Problems to be Solved by the Invention] Furthermore, as a method for adjusting the flow rate of a septic tank without a flow rate adjustment function, there is a method that utilizes water level fluctuations in an anaerobic filter bed tank.

【0005】水位変動により行う調整方法として、嫌気
濾床槽第2室30から接触曝気槽40への移流管を設け
ずに、図4に示すように、少流量ずつ接触曝気槽40に
送る定量ポンプ36を取り付け、嫌気濾床槽第2室30
の水位を変動させる方式がある。この場合、嫌気濾床槽
第1室20を出た処理水は、移流管30aを下降して、
濾材32を上向き流で通過する。そして、定量ポンプ3
6の作動により、嫌気濾床槽第2室30内の処理水は、
流入水(矢印C)と接触曝気槽40への流量(矢印A)
により、最高水位HWLと最低水位LWLとの間で変動
する。しかし、この方式では、濾材32の上に定量ポン
プ36が配置され、嫌気濾床槽第2室30の水の流れが
上向き流であるから、嫌気濾床槽第2室30は、嫌気濾
床槽第2室30の水位変動分、すなわち最低水位LWL
から最高水位HWLまでの水量の影響を直接に受け、嫌
気濾床槽第2室30の機能が安定しない。
[0005] As an adjustment method based on water level fluctuations, without providing an advection pipe from the second chamber 30 of the anaerobic filter bed tank to the contact aeration tank 40, a fixed amount is sent to the contact aeration tank 40 in small amounts as shown in FIG. Attach the pump 36 to the anaerobic filter bed tank second chamber 30
There is a method of varying the water level. In this case, the treated water leaving the anaerobic filter bed tank first chamber 20 descends through the advection pipe 30a,
It passes through the filter medium 32 in an upward flow. And metering pump 3
6, the treated water in the second chamber 30 of the anaerobic filter bed tank is
Inflow water (arrow C) and flow rate to contact aeration tank 40 (arrow A)
Therefore, the water level fluctuates between the highest water level HWL and the lowest water level LWL. However, in this system, the metering pump 36 is disposed above the filter medium 32, and the flow of water in the second chamber 30 of the anaerobic filter bed tank is an upward flow. Water level fluctuation in the second tank chamber 30, that is, the lowest water level LWL
The function of the second chamber 30 of the anaerobic filter bed tank is not stable as it is directly affected by the amount of water from HWL to the highest water level HWL.

【0006】本発明は、浄化槽にかかる多量な流入水が
接触曝気槽に及ぼす恐れのある悪影響を嫌気濾床槽の水
位変動により吸収し、嫌気濾床槽から出る処理水を多量
な流入水により乱さない浄化槽を提供することを目的と
している。
[0006] The present invention absorbs the adverse effects that a large amount of inflow water to the septic tank may have on the contact aeration tank by changing the water level of the anaerobic filter bed tank, and uses the large amount of inflow water to absorb the treated water coming out of the anaerobic filter bed tank. The purpose is to provide an undisturbed septic tank.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
に、本発明の浄化槽においては、嫌気濾床槽第2室にお
いて接触曝気槽への移流管内に定量ポンプを設け、該嫌
気濾床槽第2室の濾材中の水の流れを下向き流にした。
[Means for Solving the Problems] In order to achieve the above object, in the septic tank of the present invention, a metering pump is provided in the advection pipe to the contact aeration tank in the second chamber of the anaerobic filter bed tank, and the anaerobic filter bed tank The flow of water in the filter medium of the second chamber was made downward.

【0008】すなわち、本発明の方法では、順次配置さ
れた嫌気濾床槽第1室(または沈澱分離槽)と、嫌気濾
床槽第2室と、接触曝気槽と、沈澱槽と、消毒槽とを有
する家庭用小形合併浄化槽の流量調整を嫌気濾床槽の水
位変動により行う運転方法において、嫌気濾床槽第2室
から処理水を接触曝気槽に移送する流量調整ポンプを嫌
気濾床槽第2室から接触曝気槽への移流管内に設けて、
流入水に応じて流量調整ポンプを作動する。
That is, in the method of the present invention, an anaerobic filter bed tank first chamber (or sedimentation separation tank), an anaerobic filter bed tank second chamber, a contact aeration tank, a settling tank, and a disinfection tank are arranged in sequence. In an operating method in which the flow rate of a small domestic combined septic tank is adjusted by changing the water level of the anaerobic filter bed tank, the flow rate adjustment pump that transfers treated water from the second chamber of the anaerobic filter bed tank to the contact aeration tank is connected to the anaerobic filter bed tank. Provided in the advection pipe from the second chamber to the contact aeration tank,
The flow rate adjustment pump is operated according to the inflow water.

【0009】本発明では、嫌気濾床槽第2室の移流管内
部に取り付けた定量ポンプにより処理水を小流量ずつ接
触曝気槽に送ることにより嫌気濾床槽の水位を変動させ
るが、定量ポンプを濾材から隔離し、嫌気濾床槽第2室
の濾材中の水の流れ方を下向き流にする。これにより、
嫌気濾床槽第2室内の処理は、移流管の最低水位から最
高水位までの水量しか流入水の影響を受けないうえ、定
量ポンプの作動による影響も受けない。
In the present invention, the water level in the anaerobic filter tank is varied by sending the treated water in small amounts to the contact aeration tank using a metering pump installed inside the advection pipe in the second chamber of the anaerobic filter tank. is isolated from the filter medium, and the flow of water in the filter medium in the second chamber of the anaerobic filter bed tank is made downward. This results in
The treatment in the second chamber of the anaerobic filter bed tank is affected only by the amount of water flowing in from the lowest water level to the highest water level of the advection pipe, and is not affected by the operation of the metering pump.

【0010】0010

【作用】上記のように構成された浄化槽で汚水を処理す
ると、嫌気濾床槽第2室の移流管内に流量調整ポンプを
設けるので、嫌気濾床槽第1室に、短時間に大容量の汚
水流入があっても、一旦嫌気濾床槽にHWLまで貯留し
、且つ流量調整ポンプで接触曝気槽への排出を定量に維
持できる。従って、移流管内のHWLとLWLの間で水
位がわずかに変動するだけで、沈澱分離処理は安定に保
たれる。
[Operation] When wastewater is treated in the septic tank configured as described above, a flow rate adjustment pump is installed in the advection pipe of the second chamber of the anaerobic filter tank, so a large capacity can be transferred to the first chamber of the anaerobic filter tank in a short period of time. Even if sewage flows in, it can be stored up to HWL in the anaerobic filter bed tank, and the discharge to the contact aeration tank can be maintained at a fixed amount using the flow rate adjustment pump. Therefore, the precipitation separation process can be kept stable with only slight fluctuations in the water level between HWL and LWL in the advection tube.

【0011】本発明は、嫌気濾床槽の移流管内部に取り
付けた定量ポンプで、接触曝気槽へ一定量ずつ嫌気濾床
槽処理水を流入させるので、嫌気濾床槽は、ポンプの作
用によって一定時間がたつと、水位が下がる。嫌気濾床
槽の水位が下がるため、排水が多量に流入しても、嫌気
濾床槽の水位が上がるだけで、接触曝気槽へ悪影響を及
ばさない。
[0011] The present invention uses a metering pump installed inside the advection pipe of the anaerobic filter bed tank to cause the anaerobic filter tank treated water to flow into the contact aeration tank in a fixed amount at a time, so that the anaerobic filter bed tank is controlled by the action of the pump. After a certain amount of time, the water level will drop. Since the water level in the anaerobic filter bed tank is lowered, even if a large amount of wastewater flows in, the water level in the anaerobic filter bed tank will only rise, and the contact aeration tank will not be adversely affected.

【0012】また、嫌気濾床槽の濾材を接触曝気槽への
移流管から分離し、濾材における水の流れ方を下向き流
にすることにより、嫌気濾床槽が受ける流入水からの影
響は、嫌気濾床槽の移流管内の最低水位から最高水位ま
での水量に収まり、流入水やこれに伴う移流管内のポン
プの作動の大きな影響を受けないので、嫌気濾床槽第2
室の機能が安定する。
Furthermore, by separating the filter medium of the anaerobic filter bed tank from the advection pipe to the contact aeration tank and making the water flow in the filter medium downward, the influence of inflow water on the anaerobic filter bed tank can be reduced. The amount of water falls within the range from the lowest water level to the highest water level in the advection pipe of the anaerobic filter tank, and is not significantly affected by inflow water or the associated operation of the pump in the advection pipe, so the second anaerobic filter bed tank
The function of the room becomes stable.

【0013】[0013]

【実施例】家庭用合併処理槽に本発明を適用した実施例
について図面を参照して説明する。
[Embodiment] An embodiment in which the present invention is applied to a household combined treatment tank will be described with reference to the drawings.

【0014】図1〜図2は、一家庭用合併浄化槽に本発
明を適用した実施例を示す概念図である。
FIGS. 1 and 2 are conceptual diagrams showing an embodiment in which the present invention is applied to a combined septic tank for one household.

【0015】浄化槽は、嫌気濾床槽第1室20、嫌気濾
床槽第2室30、接触曝気槽40、沈澱槽50及び消毒
槽60で構成される。嫌気濾床槽第1室20および第2
室30における処理を一次処理と呼び、接触曝気槽40
、沈澱槽50及び消毒槽60における処理を二次処理と
呼ぶ。そして、本発明では、一次処理と二次処理の間に
流量調整ポンプ36を設ける形になる。流入口21から
流入(矢印C)した汚水は嫌気濾床槽第1室20に流入
し、濾材22中を流下し、沈澱分離処理され、移流管2
4を経て連通口28から嫌気濾床槽第2室30に移流し
、濾材32中を流下し、移流管34を経て定量ポンプ移
送管38から接触曝気槽40に入る。
The septic tank is composed of an anaerobic filter bed tank first chamber 20, an anaerobic filter bed tank second chamber 30, a contact aeration tank 40, a settling tank 50, and a disinfection tank 60. Anaerobic filter bed tank first chamber 20 and second chamber
The treatment in the chamber 30 is called primary treatment, and the contact aeration tank 40
, the processing in the settling tank 50 and the disinfection tank 60 is called secondary processing. In the present invention, a flow rate adjustment pump 36 is provided between the primary treatment and the secondary treatment. Sewage flowing in from the inlet 21 (arrow C) flows into the anaerobic filter bed tank first chamber 20, flows down through the filter medium 22, is subjected to sedimentation separation treatment, and is transferred to the advection tube 2.
4, from the communication port 28 to the second chamber 30 of the anaerobic filter bed tank, flows down through the filter medium 32, passes through the advection pipe 34, and enters the contact aeration tank 40 from the metering pump transfer pipe 38.

【0016】定量ポンプ移送管38は、HWLより高い
ところにあり、移流管34内にある定量ポンプ36によ
り処理水が嫌気濾床槽第2室30から接触曝気槽40に
入る。
The metering pump transfer pipe 38 is located higher than the HWL, and the metering pump 36 in the advection pipe 34 causes the treated water to enter the contact aeration tank 40 from the second chamber 30 of the anaerobic filter bed tank.

【0017】定量排出ポンプ36には特公昭57−55
93に示されるものが使用できる。
[0017] The metering discharge pump 36 is
93 can be used.

【0018】この定量ポンプは、可動部を有さないので
浄化処理用移流装置に適し、平均に均等化した微少流量
の移送ポンプとして勝れ、さらに嫌気濾床槽で浮遊固形
物が除去されるので、適用上安全である。
Since this metering pump has no moving parts, it is suitable for use as an advection device for purification treatment, and is excellent as a transfer pump with a minute flow rate that is equalized on the average.Furthermore, suspended solids are removed in an anaerobic filter bed tank. Therefore, it is safe for application.

【0019】接触曝気槽40では、接触材42に付着生
育する生物膜によって処理水が浄化されると共に、散気
装置44により曝気処理される。すなわち、ブロア45
から散気装置44の送気管44aを介して送り込まれた
空気が、散気管44bから出て処理水を曝気処理する。
In the contact aeration tank 40, the treated water is purified by the biofilm grown on the contact material 42, and is also aerated by the aeration device 44. That is, blower 45
The air sent through the air supply pipe 44a of the aeration device 44 comes out from the aeration pipe 44b and aerates the treated water.

【0020】接触曝気された処理水は、接触曝気槽40
の底部にある連通口46から沈澱槽50に入る。接触材
42に付着肥厚した汚泥は処理水の流れで剥離して浮遊
物質(SS)となるが、剥離汚泥として沈降し、貯留さ
れる。沈澱槽50内の上澄液が消毒槽60に入る。消毒
された処理水がここから放出(矢印B)される。
The treated water subjected to contact aeration is transferred to a contact aeration tank 40.
It enters the settling tank 50 through the communication port 46 at the bottom of the tank. The thickened sludge adhering to the contact material 42 is separated by the flow of treated water and becomes suspended solids (SS), but it settles as separated sludge and is stored. The supernatant liquid in the settling tank 50 enters the disinfection tank 60. Disinfected treated water is discharged from here (arrow B).

【0021】本実施例の浄化槽の運転の一例を説明する
An example of the operation of the septic tank of this embodiment will be explained.

【0022】嫌気濾床槽第1室20への流入汚水の量を
処理水が嫌気濾床槽第1室20から連通口28を介して
嫌気濾床槽第2室30へ入り、そして、定量ポンプ36
で嫌気濾床槽第2室30から接触曝気槽40へ送られる
。接触曝気槽40から沈澱槽50に入り、消毒槽60を
経て放出される。なお、沈澱槽50と接触曝気槽40の
底部が連通しているので、沈澱槽50から接触曝気槽4
0へ汚泥が返送され、接触曝気槽内に貯留される。
The amount of sewage flowing into the first chamber 20 of the anaerobic filter bed tank is determined when the treated water enters the second chamber 30 of the anaerobic filter bed tank from the first chamber 20 of the anaerobic filter bed tank through the communication port 28, and is quantified. pump 36
The water is sent from the second chamber 30 of the anaerobic filter bed tank to the contact aeration tank 40. From the contact aeration tank 40, it enters the settling tank 50, passes through the disinfection tank 60, and is discharged. In addition, since the bottom of the settling tank 50 and the contact aeration tank 40 are in communication, there is a flow from the settling tank 50 to the contact aeration tank 4.
The sludge is returned to 0 and stored in the contact aeration tank.

【0023】本実施例では、定量ポンプ36の移送量と
流入水の差量相当分によって、HWLとLWLの間で水
位が変動する。
In this embodiment, the water level fluctuates between HWL and LWL depending on the difference between the amount of water transferred by the metering pump 36 and the amount of inflow water.

【0024】本実施例の浄化槽では、嫌気濾床槽第2室
30の移流管34内に定量ポンプ36を設けるので、短
時間に大容量の汚水流入があっても、これを嫌気濾床槽
第1室20と第2室30で吸収でき、接触曝気槽40へ
の排出が定量に維持できる。そして、嫌気濾床槽第2室
30では水位がわずか上昇するだけで、接触曝気槽40
への流入水に汚泥が混入することはない。こうして、浄
化槽に短時間にかかる多量な流入水による悪影響を嫌気
濾床の水位変動により吸収すると共に、嫌気濾床槽第2
室の濾材中の水の流れを移流管から隔離して下向き流に
することにより、嫌気濾床槽第2室は、多量な流入水や
これに伴うポンプ作動により乱されることがない。
In the septic tank of this embodiment, since the metering pump 36 is installed in the advection pipe 34 of the second chamber 30 of the anaerobic filter bed tank, even if a large amount of wastewater flows in for a short period of time, it is not possible to transfer the wastewater to the anaerobic filter bed tank. It can be absorbed in the first chamber 20 and the second chamber 30, and the discharge to the contact aeration tank 40 can be maintained at a fixed amount. In the second chamber 30 of the anaerobic filter bed tank, the water level rises only slightly, and the contact aeration tank 40
Sludge will not be mixed into the inflow water. In this way, the adverse effects of a large amount of water flowing into the septic tank in a short period of time are absorbed by the water level fluctuations in the anaerobic filter bed, and the second anaerobic filter bed
By isolating the flow of water in the filter medium of the chamber from the advection pipe and causing it to flow downward, the second chamber of the anaerobic filter bed tank is not disturbed by large amounts of inflow water or the associated pump operations.

【0025】[0025]

【発明の効果】本発明は、以上説明したように構成され
ているので、以下に記載されるような効果を奏する。
[Effects of the Invention] Since the present invention is constructed as described above, it produces the following effects.

【0026】家庭用小形合併浄化槽の流量調整を嫌気濾
床槽の水位変動により行うに際し、嫌気濾床槽第2室の
移流管内部に小流量ずつ接触曝気槽に送る定量ポンプを
取り付け、嫌気濾床槽の水位を変動させて該浄化槽への
流入水の影響を吸収する。そして、嫌気濾床槽第2室の
濾材中の水の流れ方を下向き流にすることにより、嫌気
濾床槽第2室は、移流管の最低水位から最高水位までの
水量しか影響を受けない。また嫌気濾床槽から接触曝気
槽への汚水の移流は定量ポンプを用いることにより、嫌
気濾床槽の次の接触曝気槽への汚泥の流出を防止できる
When adjusting the flow rate of a small domestic septic tank by changing the water level of the anaerobic filter tank, a metering pump is installed inside the advection pipe of the second chamber of the anaerobic filter tank to send small flow rates to the contact aeration tank. The effect of water flowing into the septic tank is absorbed by varying the water level in the floor tank. By making the flow of water in the filter medium in the second chamber of the anaerobic filter bed tank downward, the second chamber of the anaerobic filter bed tank is only affected by the amount of water from the lowest water level to the highest water level of the advection pipe. . Furthermore, by using a metering pump to advect sewage from the anaerobic filter bed tank to the contact aeration tank, it is possible to prevent sludge from flowing out to the contact aeration tank next to the anaerobic filter bed tank.

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

【図1】本発明の一実施例を適用した浄化槽を示す概略
側断面図である。
FIG. 1 is a schematic side sectional view showing a septic tank to which an embodiment of the present invention is applied.

【図2】図1の浄化槽の概略平面図である。FIG. 2 is a schematic plan view of the septic tank in FIG. 1.

【図3】従来の浄化槽の一例を示す側断面図である。FIG. 3 is a side sectional view showing an example of a conventional septic tank.

【図4】従来の浄化槽における流量調整の一例を示す側
断面図である。
FIG. 4 is a side sectional view showing an example of flow rate adjustment in a conventional septic tank.

【符号の説明】[Explanation of symbols]

20  嫌気濾床槽第1室 21  流入口 22  濾材 24  移流管 28  連通口 30  嫌気濾床槽第2室 34  移流管 36  定量ポンプ 38  定量ポンプ移送管 40  接触曝気槽 42  接触材 44  散気装置 44a  送気管 44b  散気管 46  連通口 50  沈澱槽 60  消毒槽 20 Anaerobic filter bed tank 1st room 21 Inlet 22 Filter medium 24 Advection tube 28 Communication port 30 Anaerobic filter bed tank 2nd chamber 34 Advection tube 36 Metering pump 38 Metering pump transfer pipe 40 Contact aeration tank 42 Contact material 44 Air diffuser 44a Air pipe 44b Diffuser pipe 46 Communication port 50 Sedimentation tank 60 Disinfection tank

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  順次配置された嫌気濾床槽または沈澱
分離槽と、曝気槽と、沈澱槽と、消毒槽とを有する浄化
槽の運転方法において、嫌気濾床槽または沈澱分離槽を
第1室と第2室に分離し、該第2室から処理水を曝気槽
に移送する流量調整ポンプを第2室から接触曝気槽への
移流管内に設け、第2室の処理水が下向き流で濾材を通
過したあと移流管に入った処理水を流量調整ポンプの運
転で曝気槽に移送するようにした浄化槽の運転方法。
Claim 1. A method for operating a septic tank having an anaerobic filter bed tank or a sedimentation separation tank, an aeration tank, a sedimentation tank, and a disinfection tank arranged in sequence, wherein the anaerobic filter bed tank or the sedimentation separation tank is located in a first chamber. and a second chamber, and a flow rate adjustment pump for transferring the treated water from the second chamber to the aeration tank is installed in the advection pipe from the second chamber to the contact aeration tank, so that the treated water in the second chamber flows downward into the filter medium. A method of operating a septic tank in which treated water that enters an advection pipe after passing through is transferred to an aeration tank by operating a flow rate adjustment pump.
JP03169055A 1991-06-14 1991-06-14 Operation method of septic tank Expired - Fee Related JP3120814B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03169055A JP3120814B2 (en) 1991-06-14 1991-06-14 Operation method of septic tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03169055A JP3120814B2 (en) 1991-06-14 1991-06-14 Operation method of septic tank

Publications (2)

Publication Number Publication Date
JPH04367793A true JPH04367793A (en) 1992-12-21
JP3120814B2 JP3120814B2 (en) 2000-12-25

Family

ID=15879504

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03169055A Expired - Fee Related JP3120814B2 (en) 1991-06-14 1991-06-14 Operation method of septic tank

Country Status (1)

Country Link
JP (1) JP3120814B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07124579A (en) * 1993-11-01 1995-05-16 Kirin Brewery Co Ltd Septic tank with flow rate adjustment device
JP2002119987A (en) * 2000-06-30 2002-04-23 Hitachi Chem Co Ltd Flow rate adjusting tank, anaerobic treatment tank and sewage cleaning tank

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07124579A (en) * 1993-11-01 1995-05-16 Kirin Brewery Co Ltd Septic tank with flow rate adjustment device
JP2002119987A (en) * 2000-06-30 2002-04-23 Hitachi Chem Co Ltd Flow rate adjusting tank, anaerobic treatment tank and sewage cleaning tank

Also Published As

Publication number Publication date
JP3120814B2 (en) 2000-12-25

Similar Documents

Publication Publication Date Title
LT4316B (en) Method and apparatus for sewage water treatment
US6372137B1 (en) Wastewater treatment system for maximizing effluent quality
JPH11156360A (en) Operating method of water treatment equipment
CN107986436B (en) Biological membrane-membrane biological coupling sewage treatment device
WO2021074307A1 (en) Wastewater treatment system
CN107986435A (en) A kind of efficient up-flow biological reaction apparatus and its operation method and application
KR100414688B1 (en) Foul drain processing unit and method using settling chamber and biofilm filteration aquarium
JPH04367793A (en) Flow adjustment of purification tank
JP6243804B2 (en) Membrane separation activated sludge treatment apparatus and membrane separation activated sludge treatment method
KR101817471B1 (en) Wastewater Treatment System
JPH08187494A (en) Septic tank
JP3972406B2 (en) 厨 芥 Processing device
CN207903981U (en) A kind of efficient up-flow biological reaction apparatus
JP3729585B2 (en) Wastewater treatment facility
JP2007117908A (en) Septic tank
KR20080082852A (en) Sedimentation device for wastewater treatment and wastewater treatment method using the same
JPH0639391A (en) Sewage treatment method
JPH04317796A (en) Purifying vessel for sewage and its driving method
JP2001321791A (en) How to store excess sludge
KR20190067338A (en) Device for air blower at settling tank of sewage treatment machine
KR840001104B1 (en) Apparatus for treating waste water, or sewage by aerobic processes
JP2002357200A (en) Air lift pump, flow regulating tank and septic tank provided with the same, and method for operating air lift pump
JPH04244294A (en) Sewage treatment equipment
CN208022775U (en) Biological membrane-membrane biological coupling sewage-treatment plant
KR200242952Y1 (en) Foul drain processing unit using settling chamber and biofilm filteration aquarium

Legal Events

Date Code Title Description
S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101020

Year of fee payment: 10

LAPS Cancellation because of no payment of annual fees