JPH08290184A - Septic tank - Google Patents
Septic tankInfo
- Publication number
- JPH08290184A JPH08290184A JP9501095A JP9501095A JPH08290184A JP H08290184 A JPH08290184 A JP H08290184A JP 9501095 A JP9501095 A JP 9501095A JP 9501095 A JP9501095 A JP 9501095A JP H08290184 A JPH08290184 A JP H08290184A
- Authority
- JP
- Japan
- Prior art keywords
- chamber
- activated sludge
- filter bed
- aerobic
- septic 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.)
- Pending
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
- Treatment Of Biological Wastes In General (AREA)
- Activated Sludge Processes (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、浄化槽、更に詳しく
は、家庭の便所・洗面所・風呂・厨房等から排出される
汚水を処理する、家庭用小型の浄化槽に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a septic tank, and more particularly to a small household septic tank for treating sewage discharged from a toilet, washroom, bath, kitchen or the like at home.
【0002】[0002]
【従来の技術】家庭の便所・洗面所・風呂・厨房等から
排出される汚水を処理する家庭用浄化槽は、従来、維持
管理が容易で、槽内汚泥濃度を高く保つことができ、浄
化槽の大きさを比較的小型にできる固定床式が一般的に
利用されている。そして、この固定床式浄化槽の多く
は、嫌気濾床室、好気活性汚泥室、沈殿室及び消毒室か
ら成り、通常、沈殿室上澄水の一部は嫌気濾床室へ返送
され処理されるので、循環式ともいわれる。2. Description of the Related Art Household septic tanks that treat sewage discharged from household toilets, washrooms, baths, kitchens, etc., have traditionally been easy to maintain and maintain a high sludge concentration in the tank. A fixed bed type, which can be relatively small in size, is generally used. Most of the fixed bed type septic tank is composed of an anaerobic filter bed room, an aerobic activated sludge room, a sedimentation room and a disinfection room. Usually, a part of the supernatant water of the precipitation room is returned to the anaerobic filter bed room for treatment. Therefore, it is also called a circulation type.
【0003】この方式の浄化槽では、嫌気濾床室におい
て導入された汚水の有機物が嫌気分解(メタン発酵等)
を受ける。また、沈殿室からの返送水中の硝酸イオンは
脱窒素される。次いで、好気活性汚泥室において有機物
は酸化分解され、アンモニアは硝酸化される。そして、
沈殿室において汚泥と上澄水が分離され、上澄水はその
一部が嫌気濾床室へ返送されるほかは消毒室に送られ塩
素等で滅菌処理されて放出される。近年、沈殿室の代わ
りに好気活性汚泥室内に膜分離装置を備え、膜濾過液の
一部を好気活性汚泥室へ返送する膜分離型浄化槽が、汚
水が短時間に流入しても無処理汚水の流出する危険が少
なく流量調整も不要で、槽の小型化も期待できることか
ら、検討されている(造水技術:第20巻、No.2、第65-6
8頁、1994年、特開昭61−120694号公報、特開
平2−71896号公報)。In this type of septic tank, the organic matter in the wastewater introduced into the anaerobic filter bed is anaerobically decomposed (methane fermentation, etc.).
Receive. Further, nitrate ions in the water returned from the precipitation chamber are denitrified. Next, organic matter is oxidatively decomposed and ammonia is nitrified in the aerobic activated sludge chamber. And
Sludge and supernatant water are separated in the settling chamber, and part of the supernatant water is returned to the anaerobic filter bed chamber, and also sent to the disinfection chamber where it is sterilized with chlorine or the like and discharged. In recent years, a membrane separation type septic tank equipped with a membrane separation device in the aerobic activated sludge chamber instead of the sedimentation chamber and returning a part of the membrane filtrate to the aerobic activated sludge chamber has no effect even if sewage flows in in a short time. Considering that there is little risk of treated sewage flowing out, there is no need to adjust the flow rate, and it is expected that the tank will be smaller (water production technology: Volume 20, No. 2, No. 65-6
Page 8, 1994, JP-A-61-120694 and JP-A-2-71896).
【0004】[0004]
【発明が解決しようとする課題】しかし、上記の膜分離
型浄化槽では、膜の劣化や膜の目づまりによる濾過能力
が低下したとき、浄化槽内の水位が上昇し、オーバーフ
ローする危険がある。また脱窒の目的で好気処理水を嫌
気処理室へ返送する場合、膜分離濾過液を返送すると、
流入汚水量の数倍の液を膜濾過しなければならないの
で、膜分離装置への負荷が大きく、過大な膜面積が必要
となる。本発明は、膜分離型浄化槽の利点を生かしつ
つ、上記問題を解決する浄化槽、すなわち、小型で、汚
水を高度に処理でき、汚水の短時間流入に耐える浄化槽
の提供を目的とする。However, in the above-mentioned membrane separation type septic tank, when the filtration capacity is deteriorated due to deterioration of the membrane or clogging of the membrane, there is a risk that the water level in the septic tank rises and overflows. When returning the aerobic treated water to the anaerobic treatment chamber for the purpose of denitrification, returning the membrane separation filtrate,
Since it is necessary to carry out membrane filtration of a liquid which is several times the amount of inflowing wastewater, the load on the membrane separation device is large and an excessive membrane area is required. An object of the present invention is to provide a septic tank which solves the above-mentioned problems while utilizing the advantages of the membrane separation type septic tank, that is, a small-sized septic tank capable of highly treating sewage and capable of withstanding a short-time inflow of sewage.
【0005】[0005]
【課題を解決するための手段】本発明の浄化槽は、互い
に隔壁により仕切られてなる、嫌気濾床室(第1槽)及
び散気管を配した好気活性汚泥室(第2槽)の二槽の処
理槽をもち、その好気活性汚泥室の処理水の一部は上記
嫌気濾床室へ返送され処理される浄化槽であって、その
好気活性汚泥室内には、活性汚泥液から清澄液を膜分離
し排出するための膜分離装置、と好気活性汚泥室内の液
が底部で連通可能な仕切りで仕切られ、上部には上澄液
を上記嫌気濾床室に返送する返送管が配された沈降分離
室、が設けられた浄化槽である。The septic tank of the present invention is divided into two parts, that is, an anaerobic filter bed chamber (first tank) and an aerobic activated sludge chamber (second tank) having an air diffuser, which are partitioned by a partition wall. It is a septic tank that has a tank treatment tank, and a part of the treated water in the aerobic activated sludge chamber is returned to the anaerobic filter bed chamber for treatment and is clarified from the activated sludge liquid in the aerobic activated sludge chamber. A membrane separation device for membrane separation and discharge of the liquid, and the liquid in the aerobic activated sludge chamber is partitioned by a partition that can communicate at the bottom, and a return pipe for returning the supernatant liquid to the anaerobic filter chamber at the top. It is a septic tank provided with a settling separation chamber.
【0006】また、本発明の浄化槽は、上記の構成に加
えて更に、上記嫌気濾床室の濾床下部から上記好気活性
汚泥室上部には、越流管が、その出口位置が返送管吸込
み口と同じ高さの位置となるように設けられ、かつ、沈
降分離室には返送管吸込み口のレベルよりも高いレベル
に非常時用放流口、が設けられた浄化槽である。In addition to the above structure, the septic tank of the present invention further comprises an overflow pipe from the lower part of the filter bed of the anaerobic filter bed to the upper part of the aerobic activated sludge room and a return pipe at the outlet position thereof. The septic tank is provided so as to be at the same height as the suction port, and the settling separation chamber is provided with an emergency discharge port at a level higher than the level of the return pipe suction port.
【0007】本発明の浄化槽の本体はFRPやSMC等
で造られ、少なくとも、隔壁によって分けられた嫌気濾
床室(第1槽)と散気管を配した好気活性汚泥室(第2
槽)の二槽をもつ。第1槽の嫌気濾床室に流入する汚水
の固形物は濾床で捕捉され、その濾床に生息する嫌気性
菌の働きにより汚水の有機物の大半が分解される。The main body of the septic tank of the present invention is made of FRP, SMC or the like, and at least an anaerobic filter bed chamber (first tank) divided by a partition wall and an aerobic activated sludge chamber (2
It has two tanks. The solid matter of the sewage flowing into the anaerobic filter bed chamber of the first tank is captured by the filter bed, and most of the organic matter of the sewage water is decomposed by the action of anaerobic bacteria living in the filter bed.
【0008】本発明の浄化槽の第2槽である散気管をも
つ好気活性汚泥室には、膜分離装置と共に、沈降分離室
が設けられる。ここで用いられる膜分離装置としては、
平膜をもつ平膜分離装置、中空糸膜をもつ中空糸膜分離
装置等があるが、汚泥等による膜目づまりや膜間閉塞の
問題、それらの除去の容易さ等の点から、好ましくは、
平膜分離装置である。膜の材質としてプラスチック、セ
ラミック、金属等種々のものが用いられる。上記膜分離
装置は通常、膜、その支持体及び集水部等からなる単位
(これを膜モジュールという。)とその付帯装置(ポン
プ等)からなる。本発明においては、一個又は二以上の
複数個の膜モジュール、好ましくは一個又は二個の平膜
モジュールが、好気活性汚泥室の液中に垂直に立てた状
態で浸漬され、ポンプで吸引しながら処理、濾過され
る。膜濾過液(清澄液)は嫌気濾床室に返送されること
なく、次に消毒室に送られ塩素等で滅菌処理され、放流
される。In the aerobic activated sludge chamber having an air diffuser which is the second tank of the septic tank of the present invention, a sedimentation separation chamber is provided together with the membrane separation device. As the membrane separation device used here,
Although there are flat membrane separators having flat membranes, hollow fiber membrane separators having hollow fiber membranes, etc., it is preferable from the viewpoints of membrane clogging and intermembrane clogging due to sludge, etc., and their ease of removal. ,
It is a flat membrane separation device. Various materials such as plastic, ceramic, and metal are used as the material of the film. The above-mentioned membrane separation device usually comprises a unit (this is referred to as a membrane module) including a membrane, a support thereof, a water collecting portion and the like, and an auxiliary device (pump etc.) thereof. In the present invention, one or two or more membrane modules, preferably one or two flat membrane modules are immersed vertically in the liquid of the aerobic activated sludge chamber in a state of standing vertically and sucked by a pump. While being treated and filtered. The membrane filtrate (clarified liquid) is not returned to the anaerobic filter chamber, but is then sent to the disinfection chamber, sterilized with chlorine or the like, and discharged.
【0009】好気活性汚泥室内に設ける沈降分離室は、
好気活性汚泥室の一画に底部が連通する仕切り(隔壁)
で仕切ってつくることができる。沈降分離室内は、曝気
撹拌による液の流れが仕切りで遮られているので、重力
沈降による汚泥分離が起こる。ここで沈降形成される固
液界面(汚泥界面)上部の上澄液は、返送管、例えばエ
アーリフト返送管等を通じて、強制的に嫌気室へ返送さ
れる。The sedimentation separation chamber provided in the aerobic activated sludge chamber is
Partition (partition wall) whose bottom communicates with a part of the aerobic activated sludge chamber
It can be made by partitioning with. Since the flow of the liquid due to aeration and agitation is blocked by the partition in the sedimentation separation chamber, sludge separation by gravity sedimentation occurs. The supernatant of the solid-liquid interface (sludge interface) formed by sedimentation here is forcibly returned to the anaerobic chamber through a return pipe, for example, an air lift return pipe.
【0010】好気活性汚泥室に配する散気管は、膜モジ
ュールと隔壁の間であって、膜モジュールの下部に位置
する箇所に設ける。これは、曝気と撹拌の目的のほか
に、膜面に堆積する固形物を強制的に排除する役目をも
つ。The air diffuser arranged in the aerobic activated sludge chamber is provided between the membrane module and the partition wall and at a position located below the membrane module. In addition to the purpose of aeration and agitation, this has the function of forcibly removing solids deposited on the film surface.
【0011】膜分離型浄化槽は、一般的に汚水が短時間
に流入しても無処理水が排出されることはないとされる
が、膜目づまり等による濾過能力の低下とそれに起因す
る水位上昇が懸念される。そこで、本発明の浄化槽で
は、嫌気濾床室の下部から好気活性汚泥室上部にかけ
て、その出口位置が返送管吸込み口と同じ高さの位置と
なるように越流管を設けるとともに、沈降分離室には返
送管吸込み口(又は越流管出口)のレベルよりも高いレ
ベルに非常時用放流口を設ける。返送管吸込み口(又は
越流管出口)と非常時用放流口との間の容積を、流量調
整用空容積として利用し、膜目づまり等による濾過能力
の低下とそれに起因する水位上昇に備える。In a membrane separation type septic tank, it is generally said that untreated water is not discharged even if sewage flows in for a short period of time. However, deterioration of filtration capacity due to clogging of the membrane and the resulting water level. There is concern about a rise. Therefore, in the septic tank of the present invention, from the lower part of the anaerobic filter bed chamber to the upper part of the aerobic activated sludge chamber, an overflow pipe is provided so that its outlet position is at the same height as the return pipe suction port, and sedimentation separation is performed. The room will be equipped with an emergency outlet at a level higher than the level of the return pipe inlet (or overflow pipe outlet). The volume between the return pipe suction port (or the overflow pipe outlet) and the emergency discharge port is used as an empty volume for flow rate adjustment to prepare for the decrease in filtration capacity due to membrane clogging and the resulting rise in water level. .
【0012】また、返送管の吸込み口のレベルを調整す
れば、好気活性汚泥室の活性汚泥濃度を数千ppmから
数万ppmまで調整することができる。嫌気濾床室2の
濾床に捕捉堆積した余剰汚泥又は好気活性汚泥室内に蓄
積した余剰汚泥は、1年に約1回の頻度で引き抜き、適
正に汚泥管理をする。By adjusting the level of the suction port of the return pipe, the concentration of activated sludge in the aerobic activated sludge chamber can be adjusted from several thousands ppm to several tens of thousands ppm. The excess sludge captured and accumulated on the filter bed of the anaerobic filter bed chamber 2 or the excess sludge accumulated in the aerobic activated sludge room is drawn out about once a year, and the sludge is properly managed.
【0013】[0013]
【実施例】本発明の一実施例を、本発明の浄化槽の概略
構成(縦断面)を示した図1により説明する。本発明の
浄化槽は、隔壁10により仕切られた嫌気濾床室2と好
気活性汚泥室5をもっている。嫌気濾床室2へ入った汚
水は、濾床3を下降流で通過し、濾床の下部から越流管
4により好気活性汚泥室5の上部へ導かれる。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to FIG. 1 showing a schematic structure (longitudinal section) of a septic tank of the present invention. The septic tank of the present invention has an anaerobic filter bed chamber 2 and an aerobic activated sludge chamber 5 which are partitioned by a partition wall 10. The sewage that has entered the anaerobic filter bed chamber 2 passes through the filter bed 3 in a downward flow, and is guided from the lower part of the filter bed to the upper part of the aerobic activated sludge chamber 5 by an overflow pipe 4.
【0014】好気活性汚泥室5には1個(又は2以上の
複数個)の平膜モジュール7が液中に垂直に立てた状態
で浸漬されている。この平膜モジュール7と隔壁10の
間であって平膜モジュール7の下部近傍には、散気管8
が設けられている。散気管8は、空気供給による好気活
性汚泥室内の好気条件化のほか、圧送された空気のエア
ーリフトによる膜面洗浄作用も担っている。平膜モジュ
ールによる濾過水量はこの膜面通過流速に比例するの
で、好気活性汚泥処理に必要な酸素量を確保しつつ曝気
して、活性汚泥液が旋回流となるように平膜モジュール
7を配置する。In the aerobic activated sludge chamber 5, one flat membrane module 7 (or a plurality of two or more flat membrane modules) is immersed vertically in the liquid. Between the flat membrane module 7 and the partition wall 10 and near the lower portion of the flat membrane module 7, an air diffuser 8
Is provided. The air diffuser 8 serves not only for aerobic conditions in the aerobic activated sludge chamber by supplying air, but also for cleaning the membrane surface by the air lift of the air fed under pressure. Since the amount of filtered water by the flat membrane module is proportional to the flow velocity through the membrane surface, the flat membrane module 7 is set so that the activated sludge liquid becomes a swirl flow while aerating while securing the oxygen amount necessary for aerobic activated sludge treatment. Deploy.
【0015】平膜モジュールは、吸引ポンプ11により
吸引して減圧となし、膜濾過水を得る。得られた膜濾過
水は塩素等の滅菌処理を施した上で、排出する。The flat sheet membrane module is sucked by the suction pump 11 to reduce the pressure to obtain membrane filtered water. The membrane-filtered water obtained is sterilized with chlorine or the like and then discharged.
【0016】好気活性汚泥室5内の一画に、底部で連通
可能な仕切りで仕切られた沈降分離室6を設ける。ここ
で活性汚泥液中の汚泥フロックは自然沈降し、活性汚泥
フロック界面より上は透明な上澄み層が生じるので、沈
降形成された固液界面(汚泥界面)上部の上澄液は、空
気ブロワー13で空気を吹き込ながらエアーリフトで揚
水し、返送管を通って嫌気濾床室2へ返送される。返送
された好気活性汚泥処理水中の硝酸イオンは、嫌気濾床
室の濾床に棲息する嫌気性菌の働きで窒素ガスまで還元
・脱窒される。A settling separation chamber 6 which is partitioned by a partition which can communicate at the bottom is provided in one stroke in the aerobic activated sludge chamber 5. Here, sludge flocs in the activated sludge liquid spontaneously settle, and a transparent supernatant layer is formed above the activated sludge flocs interface. Therefore, the supernatant liquid above the solid-liquid interface (sludge interface) formed by sedimentation is the air blower 13 While being blown with air, the water is pumped by an air lift and returned to the anaerobic filter bed chamber 2 through a return pipe. Nitrate ions in the returned aerobic activated sludge treated water are reduced and denitrified to nitrogen gas by the action of anaerobic bacteria living in the filter bed of the anaerobic filter chamber.
【0017】返送管の吸込み口は流量調節水位設定最下
レベル15と同じレベルに設ける。流量調節水位設定最
上レベル16を想定し、このレベルに放流口(非常時
用)12を設け、膜目づまりによる透過水量の低下に備
える。嫌気濾床室2、好気活性汚泥室5及び沈降分離室
6の各室は隔壁又は仕切りにより流量調節水位設定最上
レベル16よりも高いレベルで仕切られているため、各
室の汚水が自由に混合されることはなく、膜目づまりに
よる透過水量の低下等の非常時であっても、沈降分離室
6の上澄み水のみが放流される。The suction port of the return pipe is provided at the same level as the flow control water level setting lowest level 15. Assuming the uppermost level 16 for setting the flow rate control water level, an outlet (for emergency) 12 is provided at this level to prepare for a decrease in the amount of permeated water due to clogging of the membrane. The anaerobic filter bed room 2, the aerobic activated sludge room 5 and the sedimentation separation room 6 are partitioned by partition walls or partitions at a level higher than the highest level 16 for setting the flow control water level, so that the sewage in each room is free. Only the supernatant water of the settling / separating chamber 6 is discharged even in an emergency, such as when the amount of permeated water is reduced due to clogging of the membrane without being mixed.
【0018】[0018]
【発明の効果】本発明の浄化槽は、小型で、汚水を高度
に処理でき、汚水の短時間流入にも耐えられる。また、
膜分離装置への負荷が軽減されているので膜濾過能力の
経年的劣化による運転トラブルが少ない。The septic tank of the present invention is small in size, can highly treat sewage, and can withstand a short time inflow of sewage. Also,
Since the load on the membrane separation device is reduced, there are few operational troubles due to deterioration of the membrane filtration capacity over time.
【図1】本発明の浄化槽の概略構成を示す図(縦断面
図)である。FIG. 1 is a diagram (longitudinal sectional view) showing a schematic configuration of a septic tank of the present invention.
1:浄化槽本体 2:嫌気濾床室 3:濾床 4:越流管 5:好気活性汚泥室 6:沈降分離室 7:平膜モジュール 8:散気管 9:返送管 10:隔壁 11:吸引ポンプ 12:非常時用
放流口 13:空気ブロワー 14:仕切り 15:流量調節水位設定最下レベル 16:流量調節水位設定最上レベル1: Main body of septic tank 2: Anaerobic filter bed 3: Filter bed 4: Overflow pipe 5: Aerobic activated sludge chamber 6: Sedimentation separation chamber 7: Flat membrane module 8: Air diffusion pipe 9: Return pipe 10: Partition wall 11: Suction Pump 12: Outlet for emergency 13: Air blower 14: Partition 15: Flow control water level setting lowest level 16: Flow control water level setting highest level
Claims (2)
床室(第1槽)及び散気管を配した好気活性汚泥室(第
2槽)の二槽の処理槽をもち、その好気活性汚泥室の処
理水の一部は上記嫌気濾床室へ返送され処理される浄化
槽であって、その好気活性汚泥室内には、 活性汚泥液から清澄液を膜分離し排出するための膜分離
装置、と好気活性汚泥室内の液が底部で連通可能な仕切
りで仕切られ、上部には上澄液を上記嫌気濾床室に返送
する返送管が配された沈降分離室、が設けられた浄化
槽。1. An aerobic filter having a anaerobic filter bed chamber (first tank) and an aerobic activated sludge chamber (second tank) provided with an air diffuser, which are separated from each other by partition walls. A part of the treated water in the activated sludge chamber is a septic tank that is returned to the anaerobic filter bed chamber for treatment, and a membrane for separating the clarified liquid from the activated sludge liquid and discharging it in the aerobic activated sludge chamber. The separation device and the liquid in the aerobic activated sludge chamber are partitioned by a partition that can communicate at the bottom, and a sedimentation separation chamber with a return pipe for returning the supernatant to the anaerobic filter bed chamber is provided at the top. Septic tank.
床室(第1槽)及び散気管を配した好気活性汚泥室(第
2槽)の二槽の処理槽をもち、その好気活性汚泥室の処
理水の一部は上記嫌気濾床室へ返送され処理される浄化
槽であって、その好気活性汚泥室内には、 活性汚泥液から清澄液を膜分離し排出するための膜分離
装置、と好気活性汚泥室内の液が底部で連通可能な仕切
りで仕切られ、上部には上澄液を上記嫌気濾床室に返送
する返送管が配された沈降分離室、が設けられ、 更に、上記嫌気濾床室の濾床下部から上記好気活性汚泥
室上部には、越流管が、その出口位置が返送管吸込み口
と同じ高さの位置となるように設けられ、かつ、沈降分
離室には返送管吸込み口のレベルよりも高いレベルに非
常時用放流口、が設けられた浄化槽。2. An aerobic filter bed chamber (first tank) and an aerobic activated sludge chamber (second tank) provided with air diffusers, which are separated from each other by partition walls, and have two treatment tanks, and the aerobic gas is provided. A part of the treated water in the activated sludge chamber is a septic tank that is returned to the anaerobic filter bed chamber for treatment, and a membrane for separating the clarified liquid from the activated sludge liquid and discharging it in the aerobic activated sludge chamber. The separation device and the liquid in the aerobic activated sludge chamber are partitioned by a partition that can communicate at the bottom, and a sedimentation separation chamber with a return pipe for returning the supernatant to the anaerobic filter bed chamber is provided at the top. Further, an overflow pipe is provided from the filter bed lower part of the anaerobic filter bed chamber to the aerobic activated sludge chamber upper part so that its outlet position is at the same height as the return pipe suction port, and , A septic tank equipped with an emergency discharge port at a level higher than the level of the return pipe suction port in the sedimentation separation chamber
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9501095A JPH08290184A (en) | 1995-04-20 | 1995-04-20 | Septic tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9501095A JPH08290184A (en) | 1995-04-20 | 1995-04-20 | Septic tank |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH08290184A true JPH08290184A (en) | 1996-11-05 |
Family
ID=14125984
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9501095A Pending JPH08290184A (en) | 1995-04-20 | 1995-04-20 | Septic tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH08290184A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100422300B1 (en) * | 2001-11-30 | 2004-03-11 | 현대건설주식회사 | A Waste Water Disposal Plant for Digesting Membrane |
US6863817B2 (en) | 2002-12-05 | 2005-03-08 | Zenon Environmental Inc. | Membrane bioreactor, process and aerator |
CN107814439A (en) * | 2017-12-14 | 2018-03-20 | 凌志环保股份有限公司 | A kind of new rural village domestic sewage denitrifying-dephosphorizing purifies wet land system |
CN107814467A (en) * | 2017-12-14 | 2018-03-20 | 凌志环保股份有限公司 | A kind of simple domestic sewage in rural areas wet land treating system |
CN107814468A (en) * | 2017-12-14 | 2018-03-20 | 凌志环保股份有限公司 | A kind of domestic sewage in rural areas purifies wet land system |
CN108467172A (en) * | 2018-05-30 | 2018-08-31 | 芜湖优聚塑模有限公司 | A kind of modified three-grid septic tank |
CN111977913A (en) * | 2020-09-07 | 2020-11-24 | 安徽清扬水处理设备科技有限公司 | Domestic sewage divides matter multi-stage treatment device |
-
1995
- 1995-04-20 JP JP9501095A patent/JPH08290184A/en active Pending
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100422300B1 (en) * | 2001-11-30 | 2004-03-11 | 현대건설주식회사 | A Waste Water Disposal Plant for Digesting Membrane |
US6863817B2 (en) | 2002-12-05 | 2005-03-08 | Zenon Environmental Inc. | Membrane bioreactor, process and aerator |
US7022236B2 (en) | 2002-12-05 | 2006-04-04 | Zenon Environmental Inc. | Membrane bioreactor, process and aerator |
CN107814439A (en) * | 2017-12-14 | 2018-03-20 | 凌志环保股份有限公司 | A kind of new rural village domestic sewage denitrifying-dephosphorizing purifies wet land system |
CN107814467A (en) * | 2017-12-14 | 2018-03-20 | 凌志环保股份有限公司 | A kind of simple domestic sewage in rural areas wet land treating system |
CN107814468A (en) * | 2017-12-14 | 2018-03-20 | 凌志环保股份有限公司 | A kind of domestic sewage in rural areas purifies wet land system |
CN107814439B (en) * | 2017-12-14 | 2023-09-05 | 凌志环保股份有限公司 | Novel rural domestic sewage denitrification and dephosphorization purification wetland system |
CN107814468B (en) * | 2017-12-14 | 2023-09-08 | 凌志环保股份有限公司 | Rural domestic sewage purification wetland system |
CN107814467B (en) * | 2017-12-14 | 2023-09-08 | 凌志环保股份有限公司 | Simple rural domestic sewage wetland treatment system |
CN108467172A (en) * | 2018-05-30 | 2018-08-31 | 芜湖优聚塑模有限公司 | A kind of modified three-grid septic tank |
CN111977913A (en) * | 2020-09-07 | 2020-11-24 | 安徽清扬水处理设备科技有限公司 | Domestic sewage divides matter multi-stage treatment device |
CN111977913B (en) * | 2020-09-07 | 2021-05-04 | 安徽清扬水处理设备科技有限公司 | Domestic sewage divides matter multi-stage treatment device |
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