JPH11267680A - Sewage treatment equipment - Google Patents
Sewage treatment equipmentInfo
- Publication number
- JPH11267680A JPH11267680A JP7865998A JP7865998A JPH11267680A JP H11267680 A JPH11267680 A JP H11267680A JP 7865998 A JP7865998 A JP 7865998A JP 7865998 A JP7865998 A JP 7865998A JP H11267680 A JPH11267680 A JP H11267680A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- water level
- sewage treatment
- sewage
- treatment tank
- 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.)
- Withdrawn
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Biological Wastes In General (AREA)
- Activated Sludge Processes (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
(57)【要約】
【課題】 汚泥濃度を常にある一定レベル内に保ち、生
物処理の安定及び膜の保護を行う。
【解決手段】 外部から汚水が流入する夾雑物除去槽5
と、夾雑物除去槽5から供給された汚水を曝気処理する
ための汚水処理槽1とを備えた汚水浄化装置である。汚
水処理槽1内に膜処理装置2を設け、汚水処理槽1内の
膜処理装置2下方に膜処理装置2に空気を供給するため
の散気管3を配置する。膜処理槽1内の汚泥を夾雑物除
去槽5に返送するための返送ポンプ21を設けた返送管
20を具備する。汚水処理槽1における所定の処理水量
毎に返送ポンプ21を所定時間運転して汚水処理槽1内
の汚泥を夾雑物除去槽5に返送するように制御する制御
部15を設ける。
(57) [Summary] [PROBLEMS] To always maintain the sludge concentration within a certain level to stabilize biological treatment and protect a membrane. SOLUTION: A contaminant removal tank 5 into which sewage flows from outside.
And a sewage treatment tank 1 for aerating the sewage supplied from the impurity removing tank 5. A membrane treatment device 2 is provided in a sewage treatment tank 1, and an air diffuser 3 for supplying air to the membrane treatment device 2 is disposed below the membrane treatment device 2 in the sewage treatment tank 1. A return pipe 20 provided with a return pump 21 for returning sludge in the membrane treatment tank 1 to the impurity removing tank 5 is provided. A control unit (15) is provided which controls the return pump (21) for a predetermined time for each predetermined amount of treated water in the sewage treatment tank (1) to return sludge in the sewage treatment tank (1) to the impurity removing tank (5).
Description
【0001】[0001]
【発明の属する技術分野】本発明は、汚水浄化装置に関
するものである。The present invention relates to a sewage purification apparatus.
【0002】[0002]
【従来の技術】従来から図3に示すように、汚水処理槽
1内に中空糸膜のような処理膜2aを設けた膜処理装置
2を設け、汚水処理槽1内の膜処理装置2下方に膜処理
装置2に空気を供給するための散気管3を配置し、散気
管3から空気を膜処理装置2に供給することで曝気を行
って曝気処理を行い、散気管3からの空気の供給を停止
して嫌気状態として嫌気処理を行い、この曝気処理と嫌
気処理とを交互に繰り返して汚水処理を行い、更に、処
理膜2aを通過させて処理水を排出するようにした汚水
処理装置が知られている。2. Description of the Related Art Conventionally, as shown in FIG. 3, a sewage treatment tank 1 is provided with a membrane treatment apparatus 2 provided with a treatment membrane 2a such as a hollow fiber membrane. A diffuser pipe 3 for supplying air to the membrane processing apparatus 2 is disposed, and aeration is performed by supplying air from the diffuser pipe 3 to the membrane processing apparatus 2 to perform aeration processing. A sewage treatment apparatus in which the supply is stopped to perform an anaerobic treatment in an anaerobic state, the aeration treatment and the anaerobic treatment are alternately repeated to perform the sewage treatment, and the treated water is discharged through the treatment membrane 2a. It has been known.
【0003】ところが、上記のような従来例において
は、汚水処理槽1内において汚泥濃度が次第に高くな
り、汚水処理槽内における汚泥濃度をある一定レベル内
に保つことが難しく、生物処理の安定性及び処理膜の保
護の面で問題があった。そして、従来にあっては、例え
ば6ヶ月毎に汚水処理槽1内における汚泥濃度調整を行
い、汚水処理槽1の汚泥を引き抜いていた。However, in the above-described conventional example, the sludge concentration in the sewage treatment tank 1 gradually increases, and it is difficult to maintain the sludge concentration in the sewage treatment tank at a certain level. In addition, there is a problem in protection of the treated film. Conventionally, the sludge concentration in the sewage treatment tank 1 is adjusted, for example, every six months, and the sludge in the sewage treatment tank 1 is drawn out.
【0004】[0004]
【発明が解決しようとする課題】本発明は上記の従来例
の問題点に鑑みて発明したものであって、汚泥濃度を常
にある一定レベル内に保ち、生物処理の安定及び膜の保
護を行うことができる汚水浄化装置を提供することを課
題とするものである。SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems of the prior art, and keeps the sludge concentration within a certain level at all times to stabilize biological treatment and protect the membrane. It is an object of the present invention to provide a sewage purification device capable of performing the above.
【0005】[0005]
【課題を解決するための手段】上記課題を解決して本発
明の目的を達成するために、本発明の汚水浄化装置は、
外部から汚水が流入する夾雑物除去槽5と、夾雑物除去
槽5から供給された汚水を曝気処理するための汚水処理
槽1とを備えた汚水浄化装置において、汚水処理槽1内
に膜処理装置2を設け、汚水処理槽1内の膜処理装置2
下方に膜処理装置2に空気を供給するための散気管3を
配置し、膜処理槽1内の汚泥を夾雑物除去槽5に返送す
るための返送ポンプ21を設けた返送管20を具備し、
汚水処理槽1における所定の処理水量毎に返送ポンプ2
1を所定時間運転して汚水処理槽1内の汚泥を夾雑物除
去槽5に返送するように制御する制御部15を設けて成
ることを特徴とするものである。このような構成とする
ことで、汚水処理槽1内における汚泥濃度を一定に保つ
ことができることになる。In order to solve the above-mentioned problems and achieve the object of the present invention, a sewage purification apparatus of the present invention comprises:
In a sewage treatment apparatus provided with a dirt removal tank 5 into which sewage flows in from outside and a sewage treatment tank 1 for aerating the sewage supplied from the dirt removal tank 5, membrane treatment is performed in the sewage treatment tank 1. The apparatus 2 is provided, and the membrane treatment apparatus 2 in the sewage treatment tank 1 is provided.
An air diffuser 3 for supplying air to the membrane processing apparatus 2 is disposed below, and a return pipe 20 provided with a return pump 21 for returning sludge in the membrane processing tank 1 to the impurity removing tank 5 is provided. ,
Return pump 2 for each predetermined amount of treated water in sewage treatment tank 1
1 is operated for a predetermined time, and a control unit 15 for controlling the sludge in the sewage treatment tank 1 to be returned to the impurity removing tank 5 is provided. With such a configuration, the sludge concentration in the sewage treatment tank 1 can be kept constant.
【0006】また、汚水処理槽1内において曝気処理と
嫌気処理とを交互に行うように制御され、曝気処理乃至
嫌気処理の回数をカウントして処理水量を換算すること
が好ましい。このような構成とすることで、処理水量を
簡単に換算することができることになる。また、夾雑物
除去槽5内の汚水を汚水処理槽1に供給するための移送
ポンプ11を備えた移送管10を設けると共に、汚水処
理槽1に設けた膜処理装置2で処理した処理水を流出す
るための吸引ポンプ16を設けた流出管を設け、汚水処
理槽1に上限水位を検知する上限水位検知センサと、下
限水位を検知する下限水位センサ23とを設け、上限水
位検知センサで上限水位を検知して吸引ポンプ16の運
転を開始し且つ下限水位センサ23で下限水位を検知し
て吸引ポンプ16の運転を停止すると共に、下限水位を
下限水位センサ23で検知して移送ポンプ11の運転を
開始し且つ上限水位センサ22で上限水位を検知して移
送ポンプ11の運転を停止するように制御し、上限水位
センサ22における水位検知の回数をカウントして所定
回数になると返送ポンプ21を所定時間運転するように
制御する制御部15を設けることが好ましい。このよう
な構成とすることで、上限水位センサ22による上限水
位の検出の回数をカウントするという簡単な構成で、汚
泥返送に必要な処理水量を求めることができるものであ
る。Further, it is preferable that the aeration process and the anaerobic process are controlled alternately in the sewage treatment tank 1, and the number of the aeration process or the anaerobic process is counted to convert the amount of the treated water. With such a configuration, the amount of treated water can be easily converted. Further, a transfer pipe 10 provided with a transfer pump 11 for supplying sewage in the impurity removing tank 5 to the sewage treatment tank 1 is provided, and treated water treated by the membrane treatment device 2 provided in the sewage treatment tank 1 is provided. An outflow pipe provided with a suction pump 16 for outflow is provided, and an upper limit water level detection sensor for detecting an upper limit water level and a lower limit water level sensor 23 for detecting a lower limit water level are provided in the sewage treatment tank 1. The operation of the suction pump 16 is started by detecting the water level, the operation of the suction pump 16 is stopped by detecting the lower limit water level by the lower limit water level sensor 23, and the lower limit water level is detected by the lower limit water level sensor 23. The operation is started and the upper limit water level is detected by the upper limit water level sensor 22 to control the operation of the transfer pump 11 to be stopped. It is preferable to be a return pump 21 is provided a control unit 15 which controls to operate a predetermined time. With such a configuration, the amount of treated water required for returning sludge can be obtained with a simple configuration in which the number of times of detection of the upper limit water level by the upper limit water level sensor 22 is counted.
【0007】また、返送ポンプ21の運転が汚水処理槽
1における曝気処理中に行われることが好ましい。この
ような構成とすることで、曝気回流により汚水処理槽1
内の汚泥濃度が均一化されている状態で汚泥を引き抜い
て返送することができることになる。It is preferable that the operation of the return pump 21 is performed during the aeration process in the sewage treatment tank 1. With such a configuration, the sewage treatment tank 1
The sludge can be pulled out and returned in a state where the sludge concentration in the inside is uniform.
【0008】[0008]
【発明の実施の形態】以下本発明を添付図面に示す実施
形態に基づいて説明する。図1にはそれぞれ本発明の汚
水浄化装置の一実施形態の概略構成図が示してある。汚
水浄化装置は外部から汚水が流入する夾雑物除去槽5、
夾雑物除去槽5から供給された汚水を曝気処理するため
の汚水処理槽1と、汚水処理槽1で処理された処理水が
排出される消毒槽6とで構成してある。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below based on embodiments shown in the accompanying drawings. FIG. 1 is a schematic configuration diagram of one embodiment of the sewage purification apparatus of the present invention. The sewage purification device is a foreign matter removal tank 5 into which sewage flows from the outside,
The sewage treatment tank 1 for aerating the sewage supplied from the contaminant removal tank 5 and a disinfection tank 6 from which the treated water treated in the sewage treatment tank 1 is discharged.
【0009】図1に示す実施形態においては、夾雑物除
去槽5は1次夾雑物除去槽5aと2次夾雑物除去槽5b
とで構成してあり、1次夾雑物除去槽5aには家庭排水
のような排水が流入する排水流入管7が接続してあっ
て、排水流入管7から家庭排水のような汚水が1次夾雑
物除去槽5a内に流入するようになっている。1次夾雑
物除去槽5aと2次夾雑物除去槽5bにはそれぞれろ材
8が内装してあり、排水流入管7から1次夾雑物除去槽
5aに流入した汚水は1次夾雑物除去槽5a内のろ材8
により夾雑物が除去され、通水部9を経て2次夾雑物除
去槽5bに流れ、2次夾雑物除去槽5bにおいてもろ材
8により夾雑物が除去されるようになっている。In the embodiment shown in FIG. 1, the foreign matter removing tank 5 comprises a primary foreign matter removing tank 5a and a secondary foreign matter removing tank 5b.
A drainage inflow pipe 7 into which wastewater such as domestic wastewater flows is connected to the primary contaminant removal tank 5a. It flows into the impurity removing tank 5a. The primary contaminant removal tank 5a and the secondary contaminant removal tank 5b are each provided with a filter medium 8, and the wastewater flowing into the primary contaminant removal tank 5a from the drainage inflow pipe 7 is removed from the primary contaminant removal tank 5a. Filter media inside 8
Thus, the contaminants are removed, flow through the water passage section 9 to the secondary contaminant removal tank 5b, and the contaminants are removed by the filter medium 8 in the secondary contaminant removal tank 5b.
【0010】2次夾雑物除去槽5bと汚水処理槽1との
間には移送管10が設けてあって、移送管10に設けた
移送ポンプ11により2次夾雑物除去槽5bの汚水を汚
水処理装置1に移送するようになっている。汚水処理装
置1内には膜処理装置2が配置してあり、この膜処理装
置2は回流板12により囲んである。膜処理装置2の上
端及び回流板12の上端は汚水処理装置1内の最低水位
よりも下方に位置しており、また、膜処理装置2の下端
部及び回流板12は汚水処理装置1の底部よりも上方に
配置してある。汚水処理装置1の下部の膜処理装置2よ
りも下方位置には膜処理装置2に空気を供給するための
散気管3が配置してあり、空気供給装置13から空気配
管14を介して散気管3に空気が供給されるものであ
り、空気の供給は制御部15により制御される。A transfer pipe 10 is provided between the secondary contaminant removing tank 5b and the sewage treatment tank 1, and a transfer pump 11 provided in the transfer pipe 10 removes sewage from the secondary contaminant removing tank 5b into sewage. It is to be transferred to the processing device 1. A membrane treatment device 2 is disposed in the sewage treatment device 1, and the membrane treatment device 2 is surrounded by a circulation plate 12. The upper end of the membrane treatment device 2 and the upper end of the circulation plate 12 are located below the lowest water level in the sewage treatment device 1, and the lower end of the membrane treatment device 2 and the circulation plate 12 are located at the bottom of the sewage treatment device 1. It is arranged above. A diffuser 3 for supplying air to the membrane treatment device 2 is disposed below the sewage treatment device 1 and below the membrane treatment device 2, and is provided from the air supply device 13 via an air pipe 14. 3 is supplied with air, and the supply of air is controlled by the control unit 15.
【0011】そして、空気供給装置13から供給される
空気を散気管3から吐出することで膜処理装置2に空気
を供給して膜処理装置2の中空糸膜のような処理膜2a
が目詰まりしないようにすると共に汚水を回流させるこ
とで汚水を曝気処理するようになっており、この散気管
3からの空気の供給による曝気処理は後述の吸引ポンプ
16の運転時に同時に散気管3から空気を供給するよう
に設定してあり、曝気処理が終わると嫌気状態に入るよ
うになっている。Then, the air supplied from the air supply device 13 is discharged from the air diffuser 3 to supply air to the membrane processing device 2 so that the processing film 2a such as a hollow fiber membrane of the membrane processing device 2 is formed.
The sewage is aerated by circulating the sewage to prevent clogging of the sewage. The aeration by the supply of air from the diffuser 3 is performed simultaneously with the operation of the suction pump 16 described later. It is set so that air is supplied from, and enters an anaerobic state when the aeration process is completed.
【0012】膜処理装置2の処理膜2aの透過側に流出
管17の一端部を接続してあり、流出管17の他端部が
消毒槽6に接続してある。この流出管17には膜処理装
置2から処理された汚水を吸引して流出管17を介して
消毒槽6側に排出するための吸引ポンプ16が設けてあ
る。消毒槽6には消毒槽6内の消毒済みの処理水を外部
に排出するための外部排出管19が接続してある。One end of an outflow pipe 17 is connected to the permeation side of the processing membrane 2 a of the membrane processing apparatus 2, and the other end of the outflow pipe 17 is connected to the disinfection tank 6. The outflow pipe 17 is provided with a suction pump 16 for sucking the treated sewage from the membrane processing apparatus 2 and discharging the same to the disinfection tank 6 via the outflow pipe 17. An external discharge pipe 19 for discharging the sterilized treated water in the disinfection tank 6 to the outside is connected to the disinfection tank 6.
【0013】汚水処理槽1には上限水位Aと下限水位B
とが設定してあり、この上限水位Aを検出する上限水位
センサ22と下限水位を検出する下限水位センサ23と
が設けてある。上限水位センサ22、下限水位センサ2
3で検知された汚水処理槽1の水位情報は制御部15に
入力され、吸引ポンプ16や移送ポンプ11の運転を制
御するようになっている。The sewage treatment tank 1 has an upper limit water level A and a lower limit water level B
The upper limit water level sensor 22 for detecting the upper limit water level A and the lower limit water level sensor 23 for detecting the lower limit water level are provided. Upper water level sensor 22, Lower water level sensor 2
The water level information of the sewage treatment tank 1 detected in 3 is input to the control unit 15 to control the operation of the suction pump 16 and the transfer pump 11.
【0014】すなわち、汚水処理槽1内の水位が上限水
位Aとなると上限水位Aを上限水位センサ22により検
知し、制御部15からの信号で吸引ポンプ16の運転が
開始されて下限水位Bとなるまで吸引ポンプ16の運転
が継続され、下限水位センサ23により下限水位Bを検
知すると制御部15からの信号により吸引ポンプ16の
運転が停止されるように制御される。上記上限水位Aか
ら下限水位Bになるまでの間吸引ポンプ4が運転される
ことで、汚水処理槽1内の処理水が膜処理装置2の処理
膜2aを透過して流出管17を介して消毒槽6に排出さ
れる。また、上記吸引ポンプ16が運転している間散気
管3から空気が供給されるように制御部15により制御
されることで、この間は汚水処理槽1内においては曝気
処理がなされることになる。That is, when the water level in the sewage treatment tank 1 reaches the upper limit water level A, the upper limit water level A is detected by the upper limit water level sensor 22, and the operation of the suction pump 16 is started by the signal from the control unit 15, and the lower limit water level B The operation of the suction pump 16 is continued until the lower limit is reached, and when the lower limit water level B is detected by the lower limit water level sensor 23, the operation of the suction pump 16 is controlled by a signal from the control unit 15 to be stopped. By operating the suction pump 4 from the upper limit water level A to the lower limit water level B, the treated water in the sewage treatment tank 1 passes through the treatment membrane 2 a of the membrane treatment device 2 and flows through the outflow pipe 17. It is discharged to the disinfection tank 6. In addition, while the suction pump 16 is operating, the control unit 15 controls so that air is supplied from the air diffuser 3. During this time, aeration treatment is performed in the sewage treatment tank 1. .
【0015】一方、上記上限水位Aで吸引ポンプ16が
運転を開始し、下限水位Bで運転を停止するように制御
されるのであるが、汚水処理槽1内の水位が下限水位B
となると、下限水位センサ23によりこれを検知し、制
御部15からの信号により移送ポンプ11の運転が開始
され、汚水処理槽1内の水位が上限水位Aになるまでの
間移送ポンプ11の運転が継続され、上限水位センサ2
2により上限水位Aを検知すると制御部15からの信号
により移送ポンプ11の運転が停止されるように制御さ
れる。上記下限水位Bから上限水位Aになるまでの間移
送ポンプ11が運転されることで、夾雑物除去槽5内に
溜まっている汚水が汚水処理槽1内に供給される。この
間は散気管3から空気が供給されないものであって、汚
水処理槽1内においては嫌気処理がなされるものであ
る。On the other hand, the suction pump 16 is controlled so as to start operation at the upper limit water level A and to stop operation at the lower limit water level B.
When the lower limit water level sensor 23 detects this, the operation of the transfer pump 11 is started by a signal from the control unit 15 and the operation of the transfer pump 11 is continued until the water level in the sewage treatment tank 1 reaches the upper limit water level A. Is continued and the upper limit water level sensor 2
When the upper limit water level A is detected by 2, the operation of the transfer pump 11 is controlled to be stopped by a signal from the control unit 15. By operating the transfer pump 11 from the lower limit water level B to the upper limit water level A, the sewage accumulated in the impurity removing tank 5 is supplied into the sewage treatment tank 1. During this time, air is not supplied from the air diffuser 3 and anaerobic treatment is performed in the sewage treatment tank 1.
【0016】上記のように曝気処理と嫌気処理とが交互
に行われて汚水を処理し、処理水は膜処理装置2の処理
膜2aを透過することで膜処理され、流出管17を介し
て消毒槽6に排出され、更に、消毒槽6で消毒処理され
て外部排出管19から外部に排出される。ここで、本発
明においては、図1に示すように、汚水処理槽1と1次
夾雑物除去槽5aとにわたるように返送ポンプ21を備
えた返送管20が配置してある。そして、汚水処理槽1
において所定の処理水量の処理が行われる毎に制御部1
5により返送ポンプ21を所定時間運転して汚水処理槽
1内の汚泥を夾雑物除去槽5に返送するように制御して
おり、これにより汚水処理槽1内における汚泥濃度を一
定に保つようにしている。As described above, the aeration process and the anaerobic process are performed alternately to treat sewage, and the treated water is subjected to membrane treatment by passing through the treatment membrane 2 a of the membrane treatment device 2, and is passed through the outlet pipe 17. It is discharged to the disinfecting tank 6, further disinfected in the disinfecting tank 6, and discharged to the outside from the external discharge pipe 19. Here, in the present invention, as shown in FIG. 1, a return pipe 20 provided with a return pump 21 is disposed so as to extend over the sewage treatment tank 1 and the primary contaminant removal tank 5a. And sewage treatment tank 1
Each time the processing of a predetermined amount of treated water is performed in
5, the return pump 21 is operated for a predetermined time so that the sludge in the sewage treatment tank 1 is returned to the impurity removing tank 5 so that the concentration of the sludge in the sewage treatment tank 1 is kept constant. ing.
【0017】ここで、汚水処理槽1内において処理され
た所定量の汚水処理量の検出に当たっては、例えば、汚
水処理槽1内において交互に行われる曝気処理と嫌気処
理とのうち少なくともいずれか一方の処理の回数をカウ
ントすることで、汚水処理量の換算ができる。したがっ
て、曝気処理と嫌気処理とのうち少なくともいずれか一
方の処理の回数をカウントして、所定回数になると所定
の汚水処理水量に達したとみなして制御部15により返
送ポンプ21を所定時間だけ運転して汚水処理槽1内の
汚泥を夾雑物除去槽5に返送するのである。Here, in detecting the predetermined amount of sewage treated in the sewage treatment tank 1, for example, at least one of aeration treatment and anaerobic treatment alternately performed in the sewage treatment tank 1 is performed. By counting the number of times of treatment, the amount of sewage treatment can be converted. Therefore, the number of times of at least one of the aeration process and the anaerobic process is counted, and when the predetermined number of times is reached, it is considered that the predetermined amount of sewage treatment water has been reached, and the control unit 15 operates the return pump 21 for a predetermined time. Then, the sludge in the sewage treatment tank 1 is returned to the impurity removing tank 5.
【0018】曝気処理と嫌気処理とのうち少なくともい
ずれか一方の処理の回数がカウントするには、例えば、
上限水位センサ22における水位検知の回数をカウント
するものであり、所定回数になると所定の汚水処理水量
に達したとみなして制御部15により返送ポンプ21を
所定時間だけ運転して汚水処理槽1内の汚泥を夾雑物除
去槽5に返送する。この場合には上限水位センサ22に
よる上限水位の検出の回数をカウントするという簡単な
構成で、汚泥返送に必要な処理水量を求めることができ
ることになる。すなわち、図2には曝気処理と嫌気処理
との運転時間、汚水処理槽1内の水位、返送ポンプの運
転を示す一例のタイムチャートが示してあり、図2に示
す実施形態においては、1回の嫌気処理と1回の曝気処
理とを1サイクルとした場合、10サイクル目に上限水
位センサ22により上限水位Aを検知した際に一定時間
だけ返送ポンプ21をオンとして運転する例を示してい
る。In order to count the number of times of at least one of the aeration process and the anaerobic process, for example,
The upper limit water level sensor 22 counts the number of times of water level detection. When the predetermined number of times is reached, it is considered that a predetermined amount of sewage treatment water has been reached, and the return pump 21 is operated by the control unit 15 for a predetermined time and the sewage treatment tank 1 Is returned to the impurity removing tank 5. In this case, the amount of treated water required for returning the sludge can be obtained with a simple configuration in which the number of times of detection of the upper limit water level by the upper limit water level sensor 22 is counted. That is, FIG. 2 shows an example of a time chart showing the operation times of the aeration process and the anaerobic process, the water level in the sewage treatment tank 1, and the operation of the return pump. In the embodiment shown in FIG. When the anaerobic treatment and one aeration treatment are defined as one cycle, the return pump 21 is turned on for a certain period of time when the upper limit water level A is detected by the upper limit water level sensor 22 in the tenth cycle, and the operation is performed. .
【0019】ここで、返送ポンプ21の運転は曝気処理
中に行われるのが好ましい。すなわち、曝気処理中には
散気管3から空気が供給されて汚水処理槽1内において
汚水が回流しているので、汚水処理槽1内の汚泥濃度が
均一化されているので、均一な濃度の汚水を一定時間返
送することで、目的とする量の汚泥を引き抜いて返送す
ることができることになる。また、運転開始時点は図2
に示すように汚水処理槽1の上限水位の時点が好まし
い。これは、返送により水位が下がって、処理膜2aが
汚水から露出するのを防いだり、あるいは水位が低過ぎ
て汚泥が引き抜けない、あるいは引き抜くべき汚泥がな
くなるのを防ぐためである。Here, the operation of the return pump 21 is preferably performed during the aeration process. That is, during the aeration process, air is supplied from the air diffuser 3 and the sewage is circulating in the sewage treatment tank 1, so that the sludge concentration in the sewage treatment tank 1 is uniform, so that a uniform concentration of the sludge is obtained. By returning the sewage for a certain period of time, a desired amount of sludge can be pulled out and returned. The operation start time is shown in FIG.
As shown in the above, the time point of the upper limit water level of the sewage treatment tank 1 is preferable. This is to prevent the water level from dropping due to the return and prevent the treatment membrane 2a from being exposed from the sewage, or to prevent sludge from being pulled out due to the water level being too low, or from running out of sludge to be drawn out.
【0020】ところで、本発明において、返送ポンプ2
1を所定時間だけ運転して汚水処理槽1内の汚泥を夾雑
物除去槽5に返送するに当たって、返送量を現場に応じ
て調整できるようにしてもよい。すなわち、各家庭にお
いて汚水量、特に汚水濃度が異なるので、返送量を現場
毎に調整する(例えば返送ポンプ21の運転時間を調整
する)ことで、汚水処理槽1の汚泥濃度を均一化するこ
とができるものである。In the present invention, the return pump 2
When the sludge in the sewage treatment tank 1 is returned to the impurity removing tank 5 by operating the tank 1 for a predetermined time, the return amount may be adjusted according to the site. That is, since the amount of sewage, particularly the concentration of sewage, differs in each household, the amount of sewage is adjusted for each site (for example, the operation time of the return pump 21 is adjusted) to make the sludge concentration in the sewage treatment tank 1 uniform. Can be done.
【0021】[0021]
【発明の効果】本発明の請求項1記載の発明にあって
は、上述のように、汚水処理槽内に膜処理装置を設け、
汚水処理槽内の膜処理装置下方に膜処理装置に空気を供
給するための散気管を配置し、膜処理槽内の汚泥を夾雑
物除去槽に返送するための返送ポンプを設けた返送管を
具備し、汚水処理槽における所定の処理水量毎に返送ポ
ンプを所定時間運転して汚水処理槽内の汚泥を夾雑物除
去槽に返送するように制御する制御部を設けてあるの
で、汚泥濃度を常にある一定レベル内に保つことがで
き、この結果、生物処理の安定及び膜の保護を行うこと
ができるものである。According to the first aspect of the present invention, as described above, a membrane treatment device is provided in a sewage treatment tank,
A return pipe provided with a diffuser pipe for supplying air to the membrane treatment apparatus below the membrane treatment apparatus in the sewage treatment tank and a return pump for returning sludge in the membrane treatment tank to the impurity removal tank is provided. A control unit for controlling the return pump to operate for a predetermined time for each predetermined amount of treated water in the sewage treatment tank to return the sludge in the sewage treatment tank to the contaminant removal tank. It can be kept at a certain level at all times, so that the biological treatment can be stabilized and the membrane can be protected.
【0022】また、請求項2記載の発明にあっては、上
記請求項1記載の発明の効果に加えて、汚水処理槽内に
おいて曝気処理と嫌気処理とを交互に行うように制御さ
れ、曝気処理乃至嫌気処理の回数をカウントして処理水
量を換算するので、曝気処理乃至嫌気処理の回数をカウ
ントするという簡単なやり方で処理水量を簡単に換算す
ることができるものである。Further, in the invention according to claim 2, in addition to the effect of the invention described in claim 1, the aeration and anaerobic treatment are controlled to be alternately performed in the sewage treatment tank, and the aeration is performed. Since the number of times of treatment or anaerobic treatment is counted to convert the amount of treated water, the amount of treated water can be easily converted by a simple method of counting the number of times of aeration treatment or anaerobic treatment.
【0023】また、請求項3記載の発明にあっては、上
記請求項2記載の発明の効果に加えて、夾雑物除去槽内
の汚水を汚水処理槽に供給するための移送ポンプを備え
た移送管を設けると共に、汚水処理槽に設けた膜処理装
置で処理した処理水を流出するための吸引ポンプを設け
た流出管を設け、汚水処理槽に上限水位を検知する上限
水位検知センサと、下限水位を検知する下限水位センサ
とを設け、上限水位検知センサで上限水位を検知して吸
引ポンプの運転を開始し且つ下限水位センサで下限水位
を検知して吸引ポンプの運転を停止すると共に、下限水
位を下限水位センサで検知して移送ポンプの運転を開始
し且つ上限水位センサで上限水位を検知して移送ポンプ
の運転を停止するように制御し、上限水位センサにおけ
る水位検知の回数をカウントして所定回数になると返送
ポンプを所定時間運転するように制御する制御部を設け
てあるので、上限水位センサによる上限水位の検出の回
数により簡単に処理水量を求めることができるものであ
る。According to the third aspect of the present invention, in addition to the effects of the second aspect, a transfer pump for supplying sewage in the contaminant removal tank to the sewage treatment tank is provided. A transfer pipe is provided, and an outflow pipe provided with a suction pump for flowing out the treated water treated by the membrane treatment device provided in the sewage treatment tank is provided, and an upper limit water level detection sensor for detecting an upper limit water level in the sewage treatment tank, A lower limit water level sensor for detecting the lower limit water level is provided, and the upper limit water level sensor detects the upper limit level to start the operation of the suction pump, and the lower limit level sensor detects the lower limit level to stop the operation of the suction pump, The lower limit water level is detected by the lower limit water level sensor to start the operation of the transfer pump, and the upper limit water level sensor is controlled to detect the upper limit water level to stop the operation of the transfer pump. Since the count to is provided with a control unit for controlling to operate for a predetermined time and return pump a predetermined number of times, those which can be obtained easily treated water by the number of detection of the upper limit water level due to the upper limit level sensor.
【0024】また、請求項4記載の発明にあっては、上
記請求項1乃至請求項3記載のいずれかに記載の発明の
効果に加えて、返送ポンプの運転が汚水処理槽における
曝気処理中に行われるので、曝気回流により汚水処理槽
内の汚泥濃度が均一化されている状態で汚泥を引き抜い
て返送することができて、汚泥の引き抜き量が安定する
ものである。According to the fourth aspect of the present invention, in addition to the effects of the first to third aspects, the operation of the return pump is performed during the aeration process in the sewage treatment tank. Therefore, the sludge can be pulled out and returned in a state where the sludge concentration in the sewage treatment tank is made uniform by the aeration circulation, and the amount of sludge drawn out is stabilized.
【図1】本発明の一実施形態の概略構成図である。FIG. 1 is a schematic configuration diagram of an embodiment of the present invention.
【図2】本発明のタイムチャートである。FIG. 2 is a time chart of the present invention.
【図3】従来例の概略構成図である。FIG. 3 is a schematic configuration diagram of a conventional example.
1 汚水処理槽 2 膜処理装置 3 散気管 5 夾雑物除去槽 10 移送管 11 移送ポンプ 15 制御部 16 吸引ポンプ 17 返送管 20 返送管 21 返送ポンプ 22 上限水位センサ 23 下限水位センサ DESCRIPTION OF SYMBOLS 1 Sewage treatment tank 2 Membrane treatment apparatus 3 Air diffuser 5 Impurity removal tank 10 Transfer pipe 11 Transfer pump 15 Control part 16 Suction pump 17 Return pipe 20 Return pipe 21 Return pump 22 Upper limit water level sensor 23 Lower limit water level sensor
───────────────────────────────────────────────────── フロントページの続き (72)発明者 真継 伸 大阪府門真市大字門真1048番地松下電工株 式会社内 (72)発明者 加納 広志 大阪府門真市大字門真1048番地松下電工株 式会社内 (72)発明者 中岡 敬善 大阪府門真市大字門真1048番地松下電工株 式会社内 (72)発明者 山口 重行 大阪府門真市大字門真1048番地松下電工株 式会社内 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Shin Shin, 1048 Kadoma, Kadoma, Osaka Prefecture Matsushita Electric Works Co., Ltd. 72) Inventor Keiyoshi Nakaoka 1048 Kadoma Kadoma, Osaka Prefecture Matsushita Electric Works Co., Ltd. (72) Inventor Shigeyuki Yamaguchi 1048 Okadoma Kadoma Kadoma City, Osaka Matsushita Electric Works Co., Ltd.
Claims (4)
と、夾雑物除去槽から供給された汚水を曝気処理するた
めの汚水処理槽とを備えた汚水浄化装置において、汚水
処理槽内に膜処理装置を設け、汚水処理槽内の膜処理装
置下方に膜処理装置に空気を供給するための散気管を配
置し、膜処理槽内の汚泥を夾雑物除去槽に返送するため
の返送ポンプを設けた返送管を具備し、汚水処理槽にお
ける所定の処理水量毎に返送ポンプを所定時間運転して
汚水処理槽内の汚泥を夾雑物除去槽に返送するように制
御する制御部を設けて成ることを特徴とする汚水処理装
置。1. A sewage purification apparatus comprising: a dirt removal tank into which sewage flows in from the outside; and a sewage treatment tank for aerating the sewage supplied from the dirt removal tank. A treatment device is provided, and a diffuser tube for supplying air to the membrane treatment device is disposed below the membrane treatment device in the sewage treatment tank, and a return pump for returning sludge in the membrane treatment tank to the impurity removal tank is provided. A return pipe is provided, and a control unit is provided for controlling the return pump to operate for a predetermined time for each predetermined amount of treated water in the sewage treatment tank to return sludge in the sewage treatment tank to the impurity removing tank. A sewage treatment apparatus characterized by the above-mentioned.
理とを交互に行うように制御され、曝気処理乃至嫌気処
理の回数をカウントして処理水量を換算するようにした
ことを特徴とする請求項1記載の汚水処理装置。2. The method according to claim 1, wherein aeration treatment and anaerobic treatment are controlled alternately in the sewage treatment tank, and the number of aeration treatments or anaerobic treatments is counted to convert the amount of treated water. Item 2. A sewage treatment apparatus according to Item 1.
給するための移送ポンプを備えた移送管を設けると共
に、汚水処理槽に設けた膜処理装置で処理した処理水を
流出するための吸引ポンプを設けた流出管を設け、汚水
処理槽に上限水位を検知する上限水位検知センサと、下
限水位を検知する下限水位センサとを設け、上限水位検
知センサで上限水位を検知して吸引ポンプの運転を開始
し且つ下限水位センサで下限水位を検知して吸引ポンプ
の運転を停止すると共に、下限水位を下限水位センサで
検知して移送ポンプの運転を開始し且つ上限水位センサ
で上限水位を検知して移送ポンプの運転を停止するよう
に制御し、上限水位センサにおける水位検知の回数をカ
ウントして所定回数になると返送ポンプを所定時間運転
するように制御する制御部を設けて成ることを特徴とす
る請求項2記載の汚水処理装置。3. A transfer pipe provided with a transfer pump for supplying sewage in a contaminant removal tank to a sewage treatment tank, and for discharging treated water treated by a membrane treatment device provided in the sewage treatment tank. An outflow pipe provided with a suction pump is provided, and an upper limit water level detection sensor for detecting an upper limit water level and a lower limit water level sensor for detecting a lower limit water level are provided in the sewage treatment tank, and the upper limit water level sensor detects the upper limit water level and sucks. The operation of the pump is started, the lower limit water level is detected by the lower water level sensor, and the operation of the suction pump is stopped. The lower water level is detected by the lower water level sensor, and the operation of the transfer pump is started. Is controlled to stop the operation of the transfer pump upon detecting the number of times the water level is detected by the upper limit water level sensor. The sewage treatment apparatus according to claim 2, further comprising a control unit.
曝気処理中に行われることを特徴とする請求項1乃至3
記載のいずれかに記載の汚水処理装置。4. The operation of the return pump is performed during aeration treatment in the sewage treatment tank.
A sewage treatment apparatus according to any one of the preceding claims.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7865998A JPH11267680A (en) | 1998-03-26 | 1998-03-26 | Sewage treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7865998A JPH11267680A (en) | 1998-03-26 | 1998-03-26 | Sewage treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH11267680A true JPH11267680A (en) | 1999-10-05 |
Family
ID=13667997
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7865998A Withdrawn JPH11267680A (en) | 1998-03-26 | 1998-03-26 | Sewage treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH11267680A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007260620A (en) * | 2006-03-29 | 2007-10-11 | Kubota Corp | Septic tank |
| CN110540293A (en) * | 2019-08-26 | 2019-12-06 | 西安建筑科技大学 | Sewage treatment device and method suitable for large-amplitude fluctuation of water quantity |
-
1998
- 1998-03-26 JP JP7865998A patent/JPH11267680A/en not_active Withdrawn
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007260620A (en) * | 2006-03-29 | 2007-10-11 | Kubota Corp | Septic tank |
| CN110540293A (en) * | 2019-08-26 | 2019-12-06 | 西安建筑科技大学 | Sewage treatment device and method suitable for large-amplitude fluctuation of water quantity |
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